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JPH02160899A - Additive used in pulverized coal/oil mixture - Google Patents

Additive used in pulverized coal/oil mixture

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Publication number
JPH02160899A
JPH02160899A JP63315595A JP31559588A JPH02160899A JP H02160899 A JPH02160899 A JP H02160899A JP 63315595 A JP63315595 A JP 63315595A JP 31559588 A JP31559588 A JP 31559588A JP H02160899 A JPH02160899 A JP H02160899A
Authority
JP
Japan
Prior art keywords
oil
coal
pulverized coal
com
phenol
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
JP63315595A
Other languages
Japanese (ja)
Inventor
Shuichi Honjo
本荘 秀一
Yoshihisa Nishida
善久 西田
Osamu Murakami
修 村上
Tsuyoshi Fujiwara
剛志 藤原
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.)
DKS Co Ltd
Original Assignee
Dai Ichi Kogyo Seiyaku 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 Dai Ichi Kogyo Seiyaku Co Ltd filed Critical Dai Ichi Kogyo Seiyaku Co Ltd
Priority to JP63315595A priority Critical patent/JPH02160899A/en
Publication of JPH02160899A publication Critical patent/JPH02160899A/en
Pending legal-status Critical Current

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  • Emulsifying, Dispersing, Foam-Producing Or Wetting Agents (AREA)
  • Liquid Carbonaceous Fuels (AREA)

Abstract

PURPOSE:To provide the title additive capable of maintaining stability over a long period of time and preventing the adhesion of coal ash to various machinery by using as constituents a specified polyamine and a compound comprising an alkylene oxide adduct of an amine/phenol/formaldehyde condensate. CONSTITUTION:An amine (e.g. methylamine), a phenol (e.g. phenol), and formaldehyde are made to undergo condensation reaction. The condensate is subjected to addition reaction with an alkylene oxide (e.g. ethylene oxide). The title additive is produced by using the compound thus obtained [e. g. of formula I (wherein EO is -CH2-CH2-O-)] and a polyamine of formula II (wherein R1 and R3 are each 1-30C alkyl, acyl or H; R2 is 2-6C alkylene; n is 1 to 20) (e.g. tallow propylenediamine) as the essential constituents, and if necessary, incorporating a solvent, etc., therein.

Description

【発明の詳細な説明】 主1↓皇且里分立 本発明は安定性を改良し、石炭灰の各種機器への付着を
防止するための微粉炭−油混合物(以下COMと称す)
用添加剤に関するものである。
[Detailed Description of the Invention] Main 1↓ Huangyuri Separation The present invention is a pulverized coal-oil mixture (hereinafter referred to as COM) for improving stability and preventing coal ash from adhering to various equipment.
It is related to additives for use.

従来夏伎街 COMは、従来石炭粒子の沈降が生し問題となっていた
が、優れた安定剤の発明によりこれが解決され、既に電
力用の石油代替燃料として大量に生産され、燃焼に供さ
れている。
In the past, Xiaqi Street COM had problems due to sedimentation of coal particles, but this problem was solved with the invention of an excellent stabilizer, and it has already been produced in large quantities and used for combustion as an alternative fuel to petroleum for electric power. ing.

従来度仇亙q入点 しかしながら、このような従来の添加剤にあっては、C
0M中に含まれる灰分が攪拌機、C0Mポンプ、制御弁
、配管のエルボ等の混合1itvが強く生ずる所や、流
速が急変する部分に付着し、たびたびラインをとめてけ
ずり取ったり、洗浄等を実施する必要が生じ、新たな問
題が発生してきた。
However, with such conventional additives, C
The ash contained in 0M adheres to areas where strong mixing occurs, such as the stirrer, C0M pump, control valves, and elbows of piping, and to areas where the flow rate changes rapidly, and the line must be frequently stopped to scrape off or clean. The need has arisen, and new problems have arisen.

特開昭57−165490に示されたポリエーテル化合
物や特公昭60−3119に示されるポリオキシアルキ
レンアルキルフェニルエーテルのホルマリン縮合物はこ
れらの問題が発生し、このためCOMの安定性をさらに
改良し、灰付着を防止する添加剤の開発が切望されてき
た。
Polyether compounds shown in JP-A-57-165490 and formalin condensates of polyoxyalkylene alkylphenyl ethers shown in JP-A-60-3119 suffer from these problems, and therefore the stability of COM has to be further improved. , there has been a strong desire to develop additives that prevent ash adhesion.

占 ”  るための この発明は、このような従来の問題点に着目してなされ
たものである。長期間安定性を保持し、灰付着を防止す
る添加剤について鋭意研究を重ねた結果、 (A)アミン類とフェノール類とホルムアルデヒドの反
応縮合物にアルキレンオキシドを付加した化合物及び (B)−最大 %式% (R1,R3:炭素数1〜30のアルキル基またはアシ
ル基あるいは水素原子、R2:炭素数2〜6のアルキレ
ン基、n=1〜20) で示されるポリアミンを必須成分として含有する添加剤
が非常に効果を有することを見い出した。
This invention for ``divination'' was made by focusing on these conventional problems.As a result of extensive research into additives that maintain long-term stability and prevent ash adhesion, ( A) A compound obtained by adding an alkylene oxide to a reaction condensate of amines, phenols, and formaldehyde, and (B) - Maximum % formula % (R1, R3: alkyl group or acyl group or hydrogen atom having 1 to 30 carbon atoms, R2 : Alkylene group having 2 to 6 carbon atoms, n=1 to 20) It has been found that an additive containing a polyamine as an essential component is very effective.

本発明の添加剤の使用により、長期間安定でかつ灰付着
のないCOMが得られ、COMを長期間かけてタンク貯
蔵でき、又、C0Mポンプや制御弁等の各種機器への灰
付着がなく、大量製造及び燃焼が可能となった。
By using the additive of the present invention, COM that is stable for a long time and does not have ash adhesion can be obtained, COM can be stored in a tank for a long period of time, and there is no ash adhesion to various equipment such as COM pumps and control valves. , mass production and combustion became possible.

−】 る− −一 本発明に使用する添加剤の(A)成分はアミン類とフェ
ノール類とホルムアルデヒドを必須成分として、縮合し
た化合物にアルキレンオキシドを付加したものであり、
各原料は下記に示すものを用いる。
- - Component (A) of the additive used in the present invention is a condensed compound containing amines, phenols, and formaldehyde as essential components, with alkylene oxide added,
The raw materials shown below are used.

アミン類としては、メチルアミン、ブチルアミン、ラウ
リルアミン、ステアリルアミン、オレイルアミン等のア
ルキルアミンや、アニリン、ベンジルアミン、トルイジ
ン、フェニレンジアミンオフチルアミン等の芳香族アミ
ンや、シクロヘキシルアミン等の脂環族アミンや、エチ
レンジアミ、′、l・ジエチレンテトラミン。ペンタエ
チレンへキサミン等のポリアミンや、アンモニア、ビペ
ラン 、ヘキサメチレンテトラミン7工タノールアミン
等ホルマリンとの縮合反応によって、組み込むことが可
能なアミン類はすべて有用である。
Examples of amines include alkylamines such as methylamine, butylamine, laurylamine, stearylamine, and oleylamine, aromatic amines such as aniline, benzylamine, toluidine, and phenylenediamine-ophthylamine, and alicyclic amines such as cyclohexylamine. and ethylenediamine,',l-diethylenetetramine. All amines that can be incorporated by condensation reaction with formalin are useful, such as polyamines such as pentaethylenehexamine, and ammonia, viperane, hexamethylenetetramine, hexamethylenetetramine, heptanotanolamine, etc.

また、二級アミン類も、上記のアミン類と併用して用い
ることができる。
Further, secondary amines can also be used in combination with the above amines.

フェノール類としては、フェノール、アルキルフェノー
ル、クレゾール、ハイドロキノン、ナフトール1 ビス
フェノール類等フェノール性水M 基を有する化合物お
よびこれらと芳香族化合物を混合したものも用いること
ができる。
As the phenol, compounds having a phenolic water group such as phenol, alkylphenol, cresol, hydroquinone, naphthol 1 bisphenols, and mixtures thereof with aromatic compounds can also be used.

ホルムアルデヒドとしては一般に、ホルマリンやバラホ
ルムアルデヒドを用いる。他に、他のアルデヒド類、例
えば、アセトアルデヒドや、ブチルアルデヒド、ヘンズ
アルデヒドをホルムアルデヒドと併用して用いてもよい
As the formaldehyde, formalin or rose formaldehyde is generally used. In addition, other aldehydes such as acetaldehyde, butyraldehyde, and henzaldehyde may be used in combination with formaldehyde.

アルキレンオキシドとしては、エチレンオキシド、プロ
ピレンオキシド、ブチレンオキシド、スチレンオキシド
等を用いるが、エチレンオキシドが最も好ましい。また
、エチレンオキシドと他のアルキレンオキシドの共重合
物もよい。
As the alkylene oxide, ethylene oxide, propylene oxide, butylene oxide, styrene oxide, etc. are used, but ethylene oxide is most preferred. Copolymers of ethylene oxide and other alkylene oxides may also be used.

次に、本発明の添加剤の製造方法は、一般には、アミン
類とフェノール類とホルムアルデヒドを無触媒あるいは
酸又は塩基性触媒の共存下で縮合せしめ、縮合後、塩水
操作を行い1.アルキレンオキシドを付加する。モル比
は一般に、アミン類とフェノール類はl/10〜10/
1、好ましくは115〜3/1である。(アミン類+フ
ェノール類)とホルムアルデヒドのモル比は、115〜
5/1、好ましくは1/3〜3/1である。
Next, the method for producing the additive of the present invention generally involves condensing amines, phenols, and formaldehyde without a catalyst or in the presence of an acid or basic catalyst, and after the condensation, a brine operation is performed.1. Add alkylene oxide. Generally, the molar ratio of amines and phenols is 1/10 to 10/1
1, preferably 115 to 3/1. The molar ratio of (amines + phenols) and formaldehyde is 115~
The ratio is 5/1, preferably 1/3 to 3/1.

アルキレンオキシドの含有率は、20〜99重量%であ
り、特にエチレンオキシドとして、30〜90重量%含
まれているものが好ましい。
The content of alkylene oxide is 20 to 99% by weight, and particularly preferably 30 to 90% by weight of ethylene oxide.

次に、(B)成分に示されるポリアミンとは、エチレン
ジアミン、牛脂プロピレンジアミン、トリエチレンテト
ラミン2 テトラエチレンペンタミン、ペンタエチレン
へキサミン等のポリアミン単独あるいはその誘導体であ
る。誘導体とは、アルキルハライドとの反応生成物、例
えばドデシルプロピレンジアミン、ドデシルトリエチレ
ンテトラミン、牛脂ジプロピレントリアミン等である。
Next, the polyamine shown as component (B) is a polyamine alone or a derivative thereof, such as ethylene diamine, tallow propylene diamine, triethylene tetramine, tetraethylene pentamine, and pentaethylene hexamine. Derivatives are reaction products with alkyl halides, such as dodecylpropylene diamine, dodecyltriethylenetetramine, tallow dipropylenetriamine, and the like.

また、ポリアミンと脂肪酸、例えばオクチル酸、ステア
リン酸、オレイン酸、特にやし油脂肪酸、牛脂脂肪酸と
のアミド化物が有効である。
Also effective are amides of polyamines and fatty acids, such as octyl acid, stearic acid, and oleic acid, especially coconut oil fatty acids and beef tallow fatty acids.

本発明のポリエーテル(A)とポリアミン(B)の配合
比は、A/B=9515〜5/95、好ましくは90/
l O〜50150である。
The blending ratio of polyether (A) and polyamine (B) of the present invention is A/B=9515 to 5/95, preferably 90/
lO~50150.

COMに用いる石炭としては、例えば無煙炭瀝青炭、亜
瀝青炭、褐炭等の各種石炭が利用でき、種類や産地にか
かわりなく、または化学組成や水分含有量にもかかわり
なく、いかなるものも利用できる。かかる石炭をそのま
ま、あるいは粗砕して油中に入れ、各種湿式粉砕機によ
り油中で直接微粉炭とするか、または通常の乾式粉砕機
により微粉炭としてもよい。ただし、湿式の粉砕法の方
が、COMの安定性が向上し、かつ粉砕時の自然発火や
粉じんが防止できるためさらによい。石炭中の水分は乾
式粉砕時に除いても、あるいは湿式粉砕中や粉砕後に砕
いてもよく、含有水分の少ないものは除かな(でも支障
がない。微粉炭の粒度は、燃焼性より判断して通常平均
粒子径200ミクロン以下のものが好ましく、更に粒度
の小さい100ミクロン以下が好適であるが、COMの
安定性等の物性に関する附り、さらに粒度の大きいもの
でも問題はない。この微粉体の含有量は、最終混合物に
対して20〜70重量%であり、70%以上の微粉炭を
含有した場合は粘度が著しく高くなり、流動性を失うた
め好ましくなく、20%以下の場合は微粉炭含有に伴う
経済面の利点が減少するため好ましくない。したがって
、20〜70重量%含有できるが、30〜60重量%が
さらに好ましい。
As the coal used for COM, various coals such as anthracite bituminous coal, sub-bituminous coal, lignite coal, etc. can be used, and any coal can be used regardless of the type or production area, or regardless of the chemical composition or moisture content. Such coal may be directly pulverized coal as it is or after being coarsely crushed and placed in oil to be pulverized coal directly in oil using various wet pulverizers, or pulverized coal may be pulverized using a conventional dry pulverizer. However, a wet pulverization method is better because it improves the stability of COM and prevents spontaneous combustion and dust during pulverization. Moisture in coal may be removed during dry pulverization, or may be crushed during wet pulverization or after pulverization, and coal with low moisture content may be removed (but there is no problem. The particle size of pulverized coal is determined based on combustibility. Normally, it is preferable to have an average particle size of 200 microns or less, and even smaller particles of 100 microns or less are preferable, but in terms of physical properties such as the stability of COM, there is no problem even with larger particle sizes. The content is 20 to 70% by weight based on the final mixture, and if it contains 70% or more of pulverized coal, the viscosity will be extremely high and fluidity will be lost, which is undesirable, and if it is less than 20%, pulverized coal will This is not preferable because the economic benefits associated with its inclusion decrease.Therefore, it can be contained in an amount of 20 to 70% by weight, but 30 to 60% by weight is more preferable.

また、COMに用いる油とは、石油原油、原油から得ら
れる各種留分、例えば灯油、軽油、へ重油、B重油、C
重油等やエチレン分解残油、クレオソート油、アントラ
セン油、各種配合油等の一般に燃料として用いられる油
や廃油、例えば、ガソリンスタンド廃油(自動車潤滑油
、洗浄油)、鉄工所廃油(機械油、切削油、洗浄油やそ
れらの混合油)、石油タンカーやその他船舶の廃油、般
化学工場廃油等をいい、それらの相互の混合物も含む。
In addition, the oil used for COM refers to petroleum crude oil, various fractions obtained from crude oil, such as kerosene, light oil, heavy oil, B heavy oil, C
Oils and waste oils commonly used as fuel such as heavy oil, ethylene decomposition residual oil, creosote oil, anthracene oil, and various blended oils, such as gas station waste oil (automobile lubricating oil, cleaning oil), ironworks waste oil (machine oil, (cutting oil, cleaning oil, and mixtures thereof), waste oil from oil tankers and other ships, waste oil from general chemical factories, etc., and also includes mixtures of these oils.

中でも石油原油およびB重油、C重油の利用が好ましい
。単独油のみ、またはあらかじめ配合した油を用いてC
OMを調製しても、単独油(好ましくは石油原油、重油
)でCOMを作った後他の油を混合したり混焼してもよ
い。
Among them, it is preferable to use petroleum crude oil, B heavy oil, and C heavy oil. C using only oil alone or pre-mixed oil
Even if OM is prepared, COM may be made from a single oil (preferably petroleum crude oil or heavy oil) and then other oils may be mixed or co-fired.

水は、石炭中に含まれる水分がC0M中に混入したり、
製造者または使用者が加える場合等があるが、水の体積
分だけ輸送費、貯蔵費、その他−般管理費が高くなり、
さらに燃焼時蒸発熱をうばい、熱損失が大きくなるため
好ましくなく、少ない方がよい。一方、水COMの安定
性を良好にする性質と、燃焼時排ガス中のNOxとバイ
ジンを少なくする効果を有するため、少量の混入は許さ
れる。したがって、全水分量は15重量%以下、好まし
くは6重量%以下がよく、全く含有しなくてもよい。
Water is caused by moisture contained in coal mixed into C0M,
There are cases where manufacturers or users add water, but transportation costs, storage costs, and other general and administrative costs will increase by the volume of water.
Furthermore, it steals the heat of vaporization during combustion and increases heat loss, which is undesirable, and the less the better. On the other hand, since it has the property of improving the stability of water COM and has the effect of reducing NOx and vizine in the exhaust gas during combustion, a small amount of water is allowed to be mixed in. Therefore, the total water content is preferably 15% by weight or less, preferably 6% by weight or less, and may not be contained at all.

本発明の添加剤を用いてCOMを安定化し、灰付着防止
効果を発揮させるには、乾式粉砕した微粉炭を油中に混
合後添加剤を加えるか、あらかじめ油中に添加剤を熔解
後乾式粉砕した微粉炭を加えるか、または微粉炭、油お
よび添加剤の王者を一括して混合すればよく、各々に水
添加を実施してもよい。また湿式粉砕の場合は、粉砕前
、粉砕中、または粉砕後のいずれの時期に添加してもよ
い。この場合も水添加を行ってもよい。
In order to stabilize COM using the additive of the present invention and exhibit the effect of preventing ash adhesion, the additive can be added after dry-pulverized pulverized coal is mixed into oil, or the additive can be melted in oil in advance and then dry-pulverized. Either pulverized pulverized coal may be added, or pulverized coal, oil and additives may be mixed all at once, and water may be added to each of them. In the case of wet pulverization, it may be added before pulverization, during pulverization, or after pulverization. In this case as well, water may be added.

混合燃料系に対する本発明添加剤の添加量は、炭種、石
炭粒度分布および油種によって若干異なるが、一般に混
合燃料中0.01〜5重量%、好ましくは0.04〜0
.8重量%であり、上限は単に経済的理由によるもので
ある。
The amount of the additive of the present invention added to the mixed fuel system varies slightly depending on the coal type, coal particle size distribution, and oil type, but is generally 0.01 to 5% by weight, preferably 0.04 to 0.0% by weight in the mixed fuel.
.. 8% by weight, the upper limit being purely for economic reasons.

本発明により、添加剤、微粉炭、油および必要により水
からなる分散系を形成する場合、任意の温度が採用され
、例えば50〜120“C″′?::混合され、混合圧
は加圧、常圧、減圧脱気時でもよく、攪拌機および攪拌
条件は、制約を受けない。
According to the invention, when forming the dispersion of additives, pulverized coal, oil and optionally water, any temperature may be employed, for example from 50 to 120 "C"'? :: The mixing pressure may be elevated pressure, normal pressure, or reduced pressure degassing, and the stirrer and stirring conditions are not restricted.

次に、本発明を実施例によりさらに詳細に説明するが、
例示は単に説明用のものであって、発明の思想を拘束す
るものではない。
Next, the present invention will be explained in more detail with reference to Examples.
The examples are merely for illustrative purposes and are not intended to constrain the spirit of the invention.

実施例 C0M製造装置の攪拌部の小規模モデルとして、特殊機
化工業−の高粘度用攪拌バネをつけたホモミキサーを使
用し、灰付着防止試験は次のように行った。
Example A homo mixer equipped with a stirring spring for high viscosity produced by Tokushu Kika Kogyo was used as a small-scale model of the stirring section of the COM manufacturing apparatus, and an ash adhesion prevention test was conducted as follows.

90℃に加温したCOM(C第1表〕に性状を示す)の
添加剤(〔第2表〕に示す)を添加し、スパチュラにて
予(!i混合を行った後、同じ温度5000rpmで1
0分間攪拌する。つづいて、攪拌機に付着したCOMを
溶剤で洗浄した後、回転部まわりに固く付着した灰分量
をall定した。この灰分量が少ない程、灰分の付着防
止性にす(れているといえる。
Add the additives (shown in Table 2) of COM (properties shown in Table 1) heated to 90°C, pre-mix with a spatula, and then mix at the same temperature of 5000 rpm. de1
Stir for 0 minutes. Subsequently, after cleaning the COM adhering to the stirrer with a solvent, the amount of ash firmly adhering around the rotating parts was determined. It can be said that the lower the ash content, the better the ash adhesion prevention properties.

また、00M安定性試験は次により行ったCOM(第1
表に性状を示す)に添加剤を0.15%加え、ホモミキ
サー4000rpmで4分間攪拌する。
In addition, the 00M stability test was conducted using the following COM (first
0.15% of the additive was added to (the properties are shown in the table) and stirred for 4 minutes with a homomixer at 4000 rpm.

攪拌したCOMを500成のポリビンに入れ、64℃の
恒温器に10日間静置する。静置(麦、ポリビンを逆さ
にしてCOMを払い出す。この時のポリビン底部に残っ
たCOMの重量、石炭濃度を測定する。
The stirred COM is placed in a 500-ml polyethylene bottle and left in a thermostat at 64°C for 10 days. Leave to stand (wheat, turn the plastic bottle upside down and take out the COM. At this time, measure the weight of the COM remaining at the bottom of the plastic bottle and the coal concentration.

結果を〔第3表〕に示す。The results are shown in [Table 3].

(以下余白) 〔第1表〕 COMの性状 〔第2表〕中の略号は下記の構造を示す。(Margin below) [Table 1] Characteristics of COM The abbreviations in [Table 2] indicate the following structures.

EO: −CH2−CH2−0−Co : −(C11
2)?CI!3C)13        C9: −(
CHz)sct13PO: −CI+2−CH−0−C
10: −(CH2)11c113CI13     
CIa : −(CH2)貸C113BO:  −CI
(2 C)12 C2:  −C11zCHa −C)I−0− C4: (CH2)3 H3
EO: -CH2-CH2-0-Co: -(C11
2)? CI! 3C) 13 C9: -(
Hz) sct13PO: -CI+2-CH-0-C
10: -(CH2)11c113CI13
CIa: -(CH2) Lending C113BO: -CI
(2 C)12 C2: -C11zCHa -C)I-0- C4: (CH2)3 H3

Claims (1)

【特許請求の範囲】 微粉炭−油混合物の安定性を改良し、微粉炭から分離し
た灰を分散させ、各種機器への灰付着を防止するために
用いる (A)アミン類とフェノール類とホルムアルデヒドの反
応縮合物にアルキレンオキシドを付加した化合物及び (B)一般式 R_1−NH−(R_2NH)_n−R_3(R_1、
R_3:炭素数1〜30のアルキル基またはアシル基あ
るいは水素原子、R_2:炭素数2〜6のアルキレン基
、n=1〜20) で示されるポリアミンを必須成分として含有することを
特徴とする微粉炭−油混合物用添加剤。
[Claims] (A) Amines, phenols, and formaldehyde used to improve the stability of a pulverized coal-oil mixture, disperse ash separated from pulverized coal, and prevent ash from adhering to various equipment. A compound obtained by adding an alkylene oxide to the reaction condensate of
R_3: an alkyl group or acyl group having 1 to 30 carbon atoms or a hydrogen atom, R_2: an alkylene group having 2 to 6 carbon atoms, n=1 to 20) A fine powder characterized by containing a polyamine as an essential component. Additive for coal-oil mixtures.
JP63315595A 1988-12-14 1988-12-14 Additive used in pulverized coal/oil mixture Pending JPH02160899A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63315595A JPH02160899A (en) 1988-12-14 1988-12-14 Additive used in pulverized coal/oil mixture

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63315595A JPH02160899A (en) 1988-12-14 1988-12-14 Additive used in pulverized coal/oil mixture

Publications (1)

Publication Number Publication Date
JPH02160899A true JPH02160899A (en) 1990-06-20

Family

ID=18067244

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63315595A Pending JPH02160899A (en) 1988-12-14 1988-12-14 Additive used in pulverized coal/oil mixture

Country Status (1)

Country Link
JP (1) JPH02160899A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2247688A (en) * 1990-09-05 1992-03-11 Sandoz Ltd Condensation products; dyeing assistants
US20120124893A1 (en) * 2009-02-16 2012-05-24 Innospec Limited Methods of treating coal to improve combustion and reduce carbon content of fly ash
WO2021226222A1 (en) * 2020-05-08 2021-11-11 Baker Hughes Oilfield Operations Llc Oxyalkylated polybenzoxazine emulsion breakers

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2247688A (en) * 1990-09-05 1992-03-11 Sandoz Ltd Condensation products; dyeing assistants
US5252104A (en) * 1990-09-05 1993-10-12 Sandoz Ltd. Products of reacting an alkylene oxide with a condensate of formaldehyde, an alkylphenol and an amine
GB2247688B (en) * 1990-09-05 1994-06-01 Sandoz Ltd Condensation products, their production and use as dyeing assistants
US20120124893A1 (en) * 2009-02-16 2012-05-24 Innospec Limited Methods of treating coal to improve combustion and reduce carbon content of fly ash
US8845767B2 (en) * 2009-02-16 2014-09-30 Innospec Limited Methods of treating coal to improve combustion and reduce carbon content of fly ash
WO2021226222A1 (en) * 2020-05-08 2021-11-11 Baker Hughes Oilfield Operations Llc Oxyalkylated polybenzoxazine emulsion breakers
US11396581B2 (en) * 2020-05-08 2022-07-26 Baker Hughes Oilfield Operations Llc Oxyalkylated polybenzoxazine emulsion breakers
GB2609372A (en) * 2020-05-08 2023-02-01 Baker Hughes Oilfield Operations Llc Oxyalkylated polybenzoxazine emulsion breakers
GB2609372B (en) * 2020-05-08 2024-04-03 Baker Hughes Oilfield Operations Llc Oxyalkylated polybenzoxazine emulsion breakers

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