JPH05178605A - Production of thermally expansible graphite - Google Patents

Production of thermally expansible graphite

Info

Publication number
JPH05178605A
JPH05178605A JP3359137A JP35913791A JPH05178605A JP H05178605 A JPH05178605 A JP H05178605A JP 3359137 A JP3359137 A JP 3359137A JP 35913791 A JP35913791 A JP 35913791A JP H05178605 A JPH05178605 A JP H05178605A
Authority
JP
Japan
Prior art keywords
drying
graphite
weight
wet cake
dried
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.)
Pending
Application number
JP3359137A
Other languages
Japanese (ja)
Inventor
Haruo Sakagami
春雄 坂上
Takeshi Suzuki
武嗣 鈴木
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.)
Nippon Kasei Chemical Co Ltd
Original Assignee
Nippon Kasei Chemical Co Ltd
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 Nippon Kasei Chemical Co Ltd filed Critical Nippon Kasei Chemical Co Ltd
Priority to JP3359137A priority Critical patent/JPH05178605A/en
Publication of JPH05178605A publication Critical patent/JPH05178605A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B32/00Carbon; Compounds thereof

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Carbon And Carbon Compounds (AREA)

Abstract

PURPOSE:To obtain thermally expansible graphite excelling in thermal stability by acid-treating graphite with a mixture of sulfuric acid and an oxidizing agent and giving it water washing and filter separation before drying it so that the ratio of the whole volatile component after drying to that before drying may be the prescribed one. CONSTITUTION:After graphite is crushed and acid-treated with a mixture of sulfuric acid and a oxidizing agent, it is washed with water and separated by filtration to obtain wet cake. Next, the wet cake is dried so that the ratio of the whole volatile component after drying to that before drying may be 60-95wt.% to get thermally expandable graphite. Here, the whole volatile component before drying is calculated by the formula, (A1-A2)/A1, where A1 grams represents the weight of a dried substance which is obtained by drying the wet cake after water washing and filter separation at 105 deg.C for 2hr and A2 grams represents the weight of the substance after heating at 1000 deg.C for 10sec. The whose volatile component after drying is calculated by the formula, (B1-B2)/B1, where B1g represents the weight of the dried sample and B2g represents the weight of the heated substance after heating at 1000 deg.C for 10sec.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、熱膨張性黒鉛の製造方
法に関する。さらに詳しくは、熱安定性に優れた熱膨張
性黒鉛の製造方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing thermally expandable graphite. More specifically, it relates to a method for producing thermally expandable graphite having excellent thermal stability.

【0002】[0002]

【従来の技術】熱膨張性黒鉛は、高温に加熱すると元の
体積の数十倍から数百倍に膨張し、これをプレスすると
可撓性に富んだ黒鉛シートが得られること、あるいはポ
リウレタンフォーム等に添加して難燃性を付与できるこ
とから工業的に重要な素材として知られている。
2. Description of the Related Art Thermally expandable graphite expands to several tens to several hundreds of its original volume when heated to a high temperature, and when it is pressed, a highly flexible graphite sheet can be obtained, or a polyurethane foam. It is known as an industrially important material because it can be added to the above to impart flame retardancy.

【0003】熱膨張性黒鉛は、通常天然黒鉛、熱分解黒
鉛、キッシュ黒鉛等の黒鉛を濃硫酸と強酸化剤との混合
物で処理(以下この処理を酸処理という)した後、水洗
し、乾燥することによって得られる。酸処理方法として
は、濃硫酸に硝酸およびその塩を用いる方法(特公昭5
4−25913号公報)、酸化剤として過マンガン酸カ
リ(特開昭55−95609号公報)、過ハロゲン酸塩
(特開昭51−96793号公報)を用いる方法、ある
いは電解反応により黒鉛の陽極酸化を行う方法(特公昭
56−18352号公報)等が知られている。
The heat-expandable graphite is usually obtained by treating natural graphite, pyrolytic graphite, quiche graphite or the like with a mixture of concentrated sulfuric acid and a strong oxidant (hereinafter this treatment is referred to as acid treatment), washing with water and drying. It is obtained by doing. As the acid treatment method, a method using nitric acid and its salt in concentrated sulfuric acid (Japanese Patent Publication No.
4-25913), a method using potassium permanganate (JP-A-55-95609) and a perhalogenate (JP-A-51-96793) as an oxidizing agent, or an anode of graphite by an electrolytic reaction. A method of performing oxidation (Japanese Patent Publication No. 56-18352) is known.

【0004】[0004]

【発明が解決しようとする課題】通常の方法で製造され
る熱膨張性黒鉛は、前記酸処理によって生成する黒鉛−
硫酸の層間化合物が水洗によって残留化合物となり、熱
膨張性を有するようになる。しかし、約200℃以上、
とりわけ約250℃以上に加熱したときに著しい加熱減
量がみられ、熱安定性が極めて悪いという特性を有す
る。このため熱膨張性黒鉛を熱可塑性樹脂等に配合する
際に、適用すべき温度に制限があるという問題点を有し
ていた。
The heat-expandable graphite produced by the usual method is the graphite produced by the acid treatment.
The intercalation compound of sulfuric acid becomes a residual compound by washing with water and becomes thermally expansive. However, about 200 ℃ or more,
In particular, when it is heated to about 250 ° C. or more, a remarkable loss on heating is observed, and it has a characteristic of extremely poor thermal stability. Therefore, there is a problem that the temperature to be applied is limited when the thermally expandable graphite is blended with the thermoplastic resin or the like.

【0005】[0005]

【課題を解決するための手段】本発明は、黒鉛を、硫酸
と酸化剤との混合物で酸処理した後、水洗、濾別、乾燥
して熱膨張性黒鉛を製造する方法において、該乾燥を濾
別後の湿潤ケーキを乾燥前の全揮発分に対して乾燥後の
全揮発分が60〜95重量%となるように実施する熱膨
張性黒鉛の製造方法を提供する、(ここで乾燥前の全揮
発分とは、水洗後濾別された湿潤ケーキを105℃で2
時間乾燥し、この乾燥物(A1g)を1000℃で10
秒間加熱した後の被加熱物の重量(A2g)とから、次
式(1) (A1−A2)/A1 (1) により算出された値であり、乾燥後の全揮発分とは、乾
燥された試料(B1g)を、1000℃で10秒間加熱
した後の被加熱物の重量(B2g)とから次式(2) (B1−B2)/B1 (2) により算出された値である。)。
The present invention provides a method for producing thermally expandable graphite by subjecting graphite to acid treatment with a mixture of sulfuric acid and an oxidizing agent, washing with water, filtering and drying. Provided is a method for producing thermally expandable graphite, wherein the wet cake after filtration is carried out such that the total volatile content after drying is 60 to 95% by weight with respect to the total volatile content before drying. The total volatile component of the wet cake was washed with water and filtered to remove the wet cake at 105 ° C.
After drying for an hour, the dried product (A 1 g) is dried at 1000 ° C. for 10
It is a value calculated by the following formula (1) (A 1 -A 2 ) / A 1 (1) from the weight (A 2 g) of the object to be heated after heating for a second, and the total volatile content after drying. Is the weight (B 2 g) of the object to be heated after heating the dried sample (B 1 g) at 1000 ° C. for 10 seconds and the following formula (2) (B 1 −B 2 ) / B 1 It is the value calculated by (2). ).

【0006】本発明者らは、250℃における加熱減量
が小さく、かつ膨張性能を損ねることのない熱膨張性黒
鉛について鋭意研究に努めた結果、特定の処理により前
記課題を解決しうることを見いだし、本発明を完成させ
た。本発明において熱膨張性黒鉛とは、天然黒鉛、熱分
解黒鉛、キッシュ黒鉛等の黒鉛を濃厚な硫酸と強い酸化
剤との混合物で酸処理した後、水洗、乾燥して得られた
ものを意味する。即ち黒鉛シート等の製造に用いられる
工業的な熱膨張性黒鉛を意味する。
The inventors of the present invention have made extensive studies as to thermally expansive graphite which has a small heating loss at 250 ° C. and does not impair the expansion performance, and as a result, found that the above-mentioned problems can be solved by a specific treatment. The present invention has been completed. In the present invention, the heat-expandable graphite means natural graphite, pyrolytic graphite, graphite obtained by acid treatment of graphite such as Kish graphite with a mixture of concentrated sulfuric acid and a strong oxidizing agent, followed by washing with water and drying. To do. That is, it means industrially thermally expandable graphite used for producing a graphite sheet or the like.

【0007】熱膨張性黒鉛は、例えば、98%硫酸と6
0%過酸化水素水の混合物中に約20〜100メッシュ
に粉砕された黒鉛を、45℃以下で10〜30分接触さ
せて酸処理を行い、その後水洗、乾燥して得られる。
The thermally expandable graphite is, for example, 98% sulfuric acid and 6%.
Graphite crushed to about 20 to 100 mesh in a mixture of 0% hydrogen peroxide water is contacted at 45 ° C. or lower for 10 to 30 minutes for acid treatment, then washed with water and dried.

【0008】水洗は、酸処理後のスラリーから硫酸等の
液相部分を分離除去し、固形分として分離された酸処理
黒鉛を多量の水中に加え、よく撹拌することにより実施
される。必要に応じ、水洗を繰り返し実施する場合もあ
る。水洗後、液相を分離除去した酸処理黒鉛は固形分と
して回収される。回収された酸処理黒鉛をアンモニア水
で中和する必要がある場合には、通常、アンモニア水を
入れた槽内に酸処理黒鉛を加えて、十分撹拌した後分離
回収する方法、水洗後に液相を分離除去する濾過工程で
残渣である回収物に直接アンモニア水を振りかけて接触
させる方法で実施される。アンモニア水の濃度は、通常
3〜4%である。水洗処理、必要に応じ中和処理して得
られた酸処理黒鉛は、棚段乾燥、気流乾燥、流動乾燥等
の方法により、通常120〜180℃程度の温度で揮発
分(105℃で2時間加熱したときの加熱減量)が1%
前後となるように乾燥される。
Washing with water is carried out by separating and removing a liquid phase portion such as sulfuric acid from the acid-treated slurry, adding the acid-treated graphite separated as a solid content to a large amount of water, and thoroughly stirring. Washing with water may be repeated if necessary. After washing with water, the acid-treated graphite from which the liquid phase has been separated and removed is recovered as a solid content. When it is necessary to neutralize the recovered acid-treated graphite with ammonia water, usually, the acid-treated graphite is added to the tank containing the ammonia water, and the mixture is thoroughly stirred and then separated and recovered. It is carried out by a method of directly sprinkling ammonia water on the recovered substance which is the residue in the filtration step of separating and removing and contacting it. The concentration of ammonia water is usually 3 to 4%. The acid-treated graphite obtained by washing with water and optionally with neutralization is subjected to volatile components (at 105 ° C. for 2 hours at a temperature of about 120 to 180 ° C.) by a method such as tray drying, air flow drying, and fluidized drying. Weight loss when heated) is 1%
It is dried to the front and back.

【0009】本発明における乾燥(以下熱処理ともい
う)とは、黒鉛を硫酸と酸化剤との混合物で酸処理した
後、水洗、濾別された湿潤ケーキを、乾燥前の全揮発分
に対し乾燥後の全揮発分が60〜95%となるように乾
燥即ち熱処理することをいう。なお乾燥前の全揮発分と
は、水洗後濾別された湿潤ケーキを105℃で2時間乾
燥し、この乾燥物(A1g)を1000℃で10秒間加
熱した後の被加熱物の重量(A2g)とから、次式
(1) (A1−A2)/A1 (1) により算出された値である。乾燥後の全揮発分とは、乾
燥された試料(B1g)を、1000℃で10秒間加熱
した後の被加熱物の重量(B2g)とから次式(2) (B1−B2)/B1 (2) により算出された値である。
In the present invention, drying (hereinafter also referred to as heat treatment) means that after acid treatment of graphite with a mixture of sulfuric acid and an oxidizing agent, the wet cake filtered and washed with water is dried with respect to all volatile components before drying. Drying or heat treatment is performed so that the total volatile content afterward becomes 60 to 95%. The total volatile matter before drying means the weight of the heated object after the wet cake filtered after washing with water is dried at 105 ° C. for 2 hours and the dried product (A 1 g) is heated at 1000 ° C. for 10 seconds. (A 2 g) is a value calculated by the following equation (1) (A 1 −A 2 ) / A 1 (1). The total volatile content after drying is calculated from the following formula (2) (B 1 −) based on the weight (B 2 g) of the object to be heated after heating the dried sample (B 1 g) at 1000 ° C. for 10 seconds. It is a value calculated by B 2 ) / B 1 (2).

【0010】なお全揮発分の測定において、約5〜10
gを試料として採取使用すると、105℃、約1時間で
揮発分が1%以下となるまで乾燥され、その後は恒量と
なり一定の値を示すので、測定用としては、試料重量5
〜10gの使用が好ましい。
In the measurement of total volatile matter, about 5-10
When g is used as a sample, it is dried at 105 ° C. for about 1 hour until the volatile content becomes 1% or less, and then it becomes a constant value and shows a constant value.
The use of 10 to 10 g is preferred.

【0011】乾燥前の全揮発分に対して乾燥後の全揮発
分が60%より小さい場合には、熱膨張性が低下し、所
望の膨張品が得られない。また95%を超える場合に
は、熱安定性が不十分となる。
When the total volatile content after drying is less than 60% with respect to the total volatile content before drying, the thermal expansion property is lowered and a desired expanded product cannot be obtained. If it exceeds 95%, the thermal stability becomes insufficient.

【0012】乾燥温度と処理時間との関係は、加熱方法
および規模に応じて適宜選択されるが、好ましくは23
0℃以上である。230℃未満の場合には、加熱時間が
長くなり経済的でない。400℃以上では、短時間処理
の場合を除き、熱膨張性黒鉛の特性である膨張性が低下
し、所望の膨張品が得られ難い。本発明の乾燥は、水洗
後液相を分離除去された酸処理黒鉛を、通常乾燥に使用
される棚段乾燥器、気流乾燥器、流動乾燥器等を用いて
実施してもよい。また本発明の乾燥を通常の乾燥条件で
ある120〜180℃で乾燥した後に実施してもよい。
The relationship between the drying temperature and the treatment time is appropriately selected according to the heating method and scale, but is preferably 23.
It is 0 ° C or higher. If the temperature is lower than 230 ° C, the heating time becomes long and it is not economical. At 400 ° C. or higher, the expansivity, which is a characteristic of the thermally expansive graphite, decreases except for the case of short-time treatment, and it is difficult to obtain a desired expanded product. The drying of the present invention may be carried out by using a tray dryer, a gas stream dryer, a fluidized dryer or the like which is usually used for drying the acid-treated graphite from which the liquid phase has been separated and removed after washing with water. Further, the drying of the present invention may be carried out after drying at 120 to 180 ° C. which is a usual drying condition.

【0013】得られた熱膨張性黒鉛が中性であることを
要求される場合には、水洗後の湿潤ケーキをアンモニア
水で、通常の乾燥工程を実施するときは該乾燥工程で、
あるいは本発明の乾燥後にアンモニアガスで中性化して
もよい。
When the obtained heat-expandable graphite is required to be neutral, the wet cake after washing with water is treated with ammonia water, and when the usual drying step is carried out, the drying step is carried out in the drying step.
Alternatively, it may be neutralized with ammonia gas after the drying of the present invention.

【0014】以下本発明を実施例に基づきより詳細に説
明する。以下の各例において測定された熱安定性および
膨張度は次のようにして測定した。 熱安定性:試料1gを坩堝に採取し、250℃に保持さ
れた恒温器中で30分間保持したときの、保持前後の重
量差を保持前の重量に対する百分率で表示した。 膨張度:1000℃に保持された電気炉内に10分以上
保持した容積120ミリリットルの石英ビーカーを炉外
に取り出し、直ちに試料0.5gを投入し、直ちに10
00℃に保持された電気炉中に入れる。そのまま10秒
間保持した後、炉外に取り出し、自然冷却した後、ビー
カーに付した目盛りによって膨張後の試料の容積を測定
する。膨張度は、試料重量に対する膨張後の容積の比
(単位:ml/g)で表示した。なお以下の各例におい
て、%はとくにことわりの無い限り重量%を示す。
Hereinafter, the present invention will be described in more detail based on examples. The thermal stability and degree of expansion measured in each of the following examples were measured as follows. Thermal stability: 1 g of a sample was sampled in a crucible and held for 30 minutes in a thermostat held at 250 ° C., and the weight difference before and after holding was expressed as a percentage of the weight before holding. Expansion degree: A quartz beaker with a volume of 120 ml, which was kept in an electric furnace maintained at 1000 ° C. for 10 minutes or more, was taken out of the furnace, and 0.5 g of a sample was immediately added to the beaker immediately.
Place in an electric furnace maintained at 00 ° C. After holding as it is for 10 seconds, the sample is taken out of the furnace, naturally cooled, and then the volume of the sample after expansion is measured by a scale attached to a beaker. The degree of expansion was expressed as the ratio of the volume after expansion to the weight of the sample (unit: ml / g). In each of the following examples,% means% by weight unless otherwise specified.

【0015】製造例 [熱膨張性黒鉛の製造]固定炭素分98%、灰分2%で
ある中国産出の天然鱗片状黒鉛(粒度:36〜80メッ
シュ)200gを98%硫酸600g、60%過酸化水
素水9.9gの混合液に加えて、30〜35℃で15分
間反応させた。反応物に1800gの58%硫酸を加え
て希釈した後、ガラス繊維濾紙(GA100)を用いて
ヌッチェで吸引濾過し、残渣を取り出した。この濾過残
渣を1600gの水中に投入し、30秒間撹拌洗浄した
後、吸引濾過して、残渣を湿潤ケーキとして分離した。
この湿潤ケーキから20gづつ7試料を分け取り、以下
の操作を実施した。なお、この湿潤ケーキ5gを熱風循
環式乾燥器中で105℃で2時間乾燥し、その0.5g
を精秤採取し、ついでこれを1000℃に保持された電
気炉内で10秒間保持した後、炉外に取り出し、自然冷
却した後、重量を測定し、全揮発分を求めたところ0.
162であった。
Production Example [Production of Thermally Expandable Graphite] 200 g of natural scaly graphite (particle size: 36 to 80 mesh) produced in China with fixed carbon content of 98% and ash content of 2% is 98% sulfuric acid 600 g, 60% peroxidation. It was added to a mixed solution of hydrogen water 9.9 g and reacted at 30 to 35 ° C. for 15 minutes. After 1800 g of 58% sulfuric acid was added to the reaction product to dilute it, suction filtration was performed with a Nutsche using a glass fiber filter paper (GA100), and the residue was taken out. The filtration residue was put into 1600 g of water, washed with stirring for 30 seconds, and then suction-filtered to separate the residue as a wet cake.
Seven samples of 20 g each were separated from this wet cake, and the following operations were performed. In addition, 0.5 g of this wet cake was dried for 2 hours at 105 ° C. in a hot air circulation dryer.
Was precisely weighed and then held in an electric furnace kept at 1000 ° C. for 10 seconds, then taken out of the furnace, naturally cooled, and then weighed to determine the total volatile content.
It was 162.

【0016】実施例1〜2 製造例で得られた湿潤ケーキ2試料について、それぞれ
約10gを、250℃、70分間(実施例1)、300
℃、35分間(実施例2)、熱風循環式乾燥器中で熱処
理を行い、それぞれの0.5gについて、1000℃に
保持された電気炉内で10秒間保持した後、炉外に取り
出し、自然冷却の後に重量を測定し、全揮発分を求め
た。
Examples 1 to 2 About 2 samples of the wet cake obtained in the production example, about 10 g of each of them was heated at 250 ° C. for 70 minutes (Example 1), 300
C., 35 minutes (Example 2), heat treatment was performed in a hot-air circulation dryer, 0.5 g of each was kept in an electric furnace kept at 1000.degree. C. for 10 seconds, then taken out of the oven, and allowed to stand naturally. After cooling, the weight was measured to determine the total volatile content.

【0017】実施例3〜4 製造例で得られた湿潤ケーキ2試料について、それぞれ
を3.7%濃度のアンモニア水60gに加え、3分間撹
拌した後、吸引濾過して分離した。各試料約10gをそ
れぞれ230℃、45分間(実施例3)、350℃、8
分間(実施例4)、熱風循環式乾燥器中で熱処理を行
い、それぞれの0.5gについて、1000℃に保持さ
れた電気炉内で10秒間保持した後、炉外に取り出し、
自然冷却の後に重量を測定し、全揮発分を求めた。
Examples 3 to 4 Two wet cake samples obtained in the production examples were added to 60 g of ammonia water having a concentration of 3.7%, stirred for 3 minutes, and then suction-filtered to separate them. About 10 g of each sample was heated at 230 ° C. for 45 minutes (Example 3), 350 ° C., 8
For 5 minutes (Example 4), heat treatment was performed in a hot air circulation dryer, and 0.5 g of each was held in an electric furnace held at 1000 ° C. for 10 seconds, and then taken out of the furnace.
After natural cooling, the weight was measured to determine the total volatile content.

【0018】比較例1〜2 製造例で得られた湿潤ケーキ2試料について、それぞれ
各試料約10gを250℃、13分間(比較例1)、3
00℃、90分間(比較例2)同様に熱処理して、全揮
発分を求めた。
Comparative Examples 1 to 2 About 2 samples of the wet cake obtained in the production example, about 10 g of each sample was 250 ° C. for 13 minutes (Comparative Example 1), 3
Heat treatment was performed in the same manner at 00 ° C. for 90 minutes (Comparative Example 2) to determine the total volatile content.

【0019】比較例3 製造例で得られた湿潤ケーキ1試料について、熱風循環
式乾燥器中で、105℃、2時間の乾燥を実施した。各
例で得られた熱処理前後の全揮発分、熱安定性、膨張度
の値を表1に示す。
Comparative Example 3 One sample of the wet cake obtained in the production example was dried at 105 ° C. for 2 hours in a hot air circulation dryer. Table 1 shows the values of total volatile matter, thermal stability, and expansion coefficient before and after heat treatment obtained in each example.

【0020】 表1 実施例 熱処理温度(℃) 250 300 230 350 熱処理時間(分) 70 35 45 8 熱処理後全揮発分 0.127 0.099 0.149 0.103 (X/Y)×100 78.4 61.1 88.3 63.6 熱安定性(%) 0.06 0.00 0.80 0.00 膨張度(ml/g) 200 180 200 190Table 1 Example 1 2 3 4 Heat treatment temperature (° C.) 250 300 300 230 350 Heat treatment time (min) 70 35 45 8 Total volatile content after heat treatment 0.127 0.099 0.149 0.103 (X / Y ) × 100 78.4 61.1 88.3 63.6 Thermal stability (%) 0.06 0.00 0.00 0.80 0.00 Expansion coefficient (ml / g) 200 180 200 200 190

【0021】 表1(続) 比較例 熱処理温度(℃) 250 300 ブランク 熱処理時間(分) 13 90 熱処理後全揮発分 0.159 0.080 (X/Y)×100 98.1 49.4 熱安定性(%) 3.02 0.00 3.94 膨張度(ml/g) 210 80 210 注: X;熱処理後の全揮発分 Y;熱処理前の全揮発分 実施例1〜4で得られた熱膨張性黒鉛は、熱処理を実施
しない比較例3に比して熱安定性が優れ、かつ膨張度は
殆ど低下していなかった。
Table 1 (continued) Comparative Example 1 2 3 Heat treatment temperature (° C.) 250 300 Blank heat treatment time (min) 13 90 Total volatile content after heat treatment 0.159 0.080 (X / Y) × 100 98.1 49 .4 Thermal stability (%) 3.02 0.00 3.9 Expansion coefficient (ml / g) 210 80 210 Note: X: Total volatiles after heat treatment Y: Total volatiles before heat treatment Examples 1-4 The heat-expandable graphite obtained in 1. had excellent thermal stability as compared with Comparative Example 3 in which heat treatment was not performed, and the expansion degree was hardly reduced.

【0022】[0022]

【発明の効果】本発明によれば、加熱減量が極めて小さ
く、熱安定性に優れた熱膨張性黒鉛が容易に得られる製
造方法が提供される。
EFFECTS OF THE INVENTION According to the present invention, there is provided a production method in which a heat loss is extremely small and a thermally expansive graphite excellent in thermal stability can be easily obtained.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 黒鉛を、硫酸と酸化剤との混合物で酸処
理した後、水洗、濾別、乾燥して熱膨張性黒鉛を製造す
る方法において、該乾燥を濾別後の湿潤ケーキを乾燥前
の全揮発分に対して乾燥後の全揮発分が60〜95重量
%となるように実施する熱膨張性黒鉛の製造方法、(こ
こで乾燥前の全揮発分とは、水洗後濾別された湿潤ケー
キを105℃で2時間乾燥し、この乾燥物(A1g)を
1000℃で10秒間加熱した後の被加熱物の重量(A
2g)とから、次式(1) (A1−A2)/A1 (1) により算出された値であり、乾燥後の全揮発分とは、乾
燥された試料(B1g)を、1000℃で10秒間加熱
した後の被加熱物の重量(B2g)とから次式(2) (B1−B2)/B1 (2) により算出された値である。)。
1. A method for producing heat-expandable graphite by subjecting graphite to acid treatment with a mixture of sulfuric acid and an oxidizing agent, washing with water, filtering and drying to dry the wet cake after filtering the drying. A method for producing heat-expandable graphite, wherein the total volatile content after drying is 60 to 95% by weight relative to the total volatile content before drying (wherein the total volatile content before drying is filtered after washing with water) The wet cake thus obtained was dried at 105 ° C. for 2 hours, and the dried product (A 1 g) was heated at 1000 ° C. for 10 seconds to obtain the weight (A
2 g) and the value calculated by the following formula (1) (A 1 −A 2 ) / A 1 (1), and the total volatile content after drying is the dried sample (B 1 g) Is the value calculated by the following equation (2) (B 1 -B 2 ) / B 1 (2) from the weight (B 2 g) of the object to be heated after heating at 1000 ° C. for 10 seconds. ).
JP3359137A 1991-12-27 1991-12-27 Production of thermally expansible graphite Pending JPH05178605A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3359137A JPH05178605A (en) 1991-12-27 1991-12-27 Production of thermally expansible graphite

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3359137A JPH05178605A (en) 1991-12-27 1991-12-27 Production of thermally expansible graphite

Publications (1)

Publication Number Publication Date
JPH05178605A true JPH05178605A (en) 1993-07-20

Family

ID=18462935

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3359137A Pending JPH05178605A (en) 1991-12-27 1991-12-27 Production of thermally expansible graphite

Country Status (1)

Country Link
JP (1) JPH05178605A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20050064539A (en) * 2003-12-24 2005-06-29 재단법인 포항산업과학연구원 Manufacturing method of exfoliated graphite from surface-treated graphite
CN100400416C (en) * 2006-07-11 2008-07-09 河北农业大学 Process for preparing expandable graphite with high reference expansion temperature
WO2022270500A1 (en) * 2021-06-22 2022-12-29 株式会社インキュベーション・アライアンス Graphene material and production method therefor

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20050064539A (en) * 2003-12-24 2005-06-29 재단법인 포항산업과학연구원 Manufacturing method of exfoliated graphite from surface-treated graphite
CN100400416C (en) * 2006-07-11 2008-07-09 河北农业大学 Process for preparing expandable graphite with high reference expansion temperature
WO2022270500A1 (en) * 2021-06-22 2022-12-29 株式会社インキュベーション・アライアンス Graphene material and production method therefor

Similar Documents

Publication Publication Date Title
US4091083A (en) Method for the production of graphite-hydrogensulfate
JPH0668025B2 (en) Purification method of polyphenylene sulfide
JPH10510797A (en) Carbon material reacted with diazonium salt
CN109641752A (en) Method for obtaining graphene oxide
WO1987005915A1 (en) Process for removing impurities from polyphenylene sulfide resin
JPS6220127B2 (en)
US4304760A (en) Method of removing potassium hydroxide from crystallized potassium ferrate (VI)
CN103058178A (en) High specific surface area graphene and preparation method and application thereof
KR970000045B1 (en) Process for selectively producing hydrate crystals
JPH05178605A (en) Production of thermally expansible graphite
Emara et al. Intermediates in the thermal decomposition of normal copper (II), nickel (II) and cobalt (II) selenite dihydrates
Willard et al. THE PREPARATION AND PROPERTIES OF MAGNESIUM PERCHLORATE AND ITS USE AS A DRYING AGENT1
JPH0664911A (en) Production of thermoexpandable graphite
JP2000044218A (en) Production of thermally expandable graphite
JPH0417883B2 (en)
JPS61126091A (en) Production of polyphosphoric acid aminotriazine compound
JPH02188418A (en) Thermally expandable graphite
KR900004489B1 (en) Process for producing aluminium nitride powder
JPH11268908A (en) Production of thermally expandable graphite
JP2004051477A (en) Method for manufacturing iron hydroxide, iron oxide hydrate or iron oxide from filtered salt of recovered diluted acid
US3933821A (en) Direct production of 1,9-anthrapyrimidine-2-carboxylic acid-1, anthraquinonylamide in pigmentary form
US2415443A (en) Strontium peroxide and method of making the same
SU1747382A1 (en) Method of preparing foamed graphite
JPH0417884B2 (en)
JPH01119511A (en) Production of high-purity boron oxide powder