JP6464377B2 - Method for dissolving polymer of carbonyl compound formed in basic washing of hydrocarbon cracking process - Google Patents

Method for dissolving polymer of carbonyl compound formed in basic washing of hydrocarbon cracking process Download PDF

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JP6464377B2
JP6464377B2 JP2014266620A JP2014266620A JP6464377B2 JP 6464377 B2 JP6464377 B2 JP 6464377B2 JP 2014266620 A JP2014266620 A JP 2014266620A JP 2014266620 A JP2014266620 A JP 2014266620A JP 6464377 B2 JP6464377 B2 JP 6464377B2
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hydroxylamine
polymer
salt
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JP2016124823A (en
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浩二 土井
浩二 土井
安夫 小谷
安夫 小谷
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Katayama Chemical Works Co Ltd
Nalco Japan GK
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    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G9/00Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
    • C10G9/14Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils in pipes or coils with or without auxiliary means, e.g. digesters, soaking drums, expansion means
    • C10G9/16Preventing or removing incrustation
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G2300/00Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/10Feedstock materials
    • C10G2300/1037Hydrocarbon fractions
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G2300/00Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/10Feedstock materials
    • C10G2300/1081Alkanes
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G2400/00Products obtained by processes covered by groups C10G9/00 - C10G69/14
    • C10G2400/20C2-C4 olefins

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  • Oil, Petroleum & Natural Gas (AREA)
  • Physics & Mathematics (AREA)
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Description

本開示は、炭化水素分解プロセスの塩基性洗浄において生成されるカルボニル化合物の重合物を溶解する方法及びそれに用いる組成物に関する。   The present disclosure relates to a method for dissolving a polymer of a carbonyl compound produced in a basic washing of a hydrocarbon cracking process and a composition used therefor.

エタン、プロパン、ブタン、ナフサ、軽油又はこれらの混合物といった炭化水素を原料とし、これらを熱分解してエチレンやプロピレン等の石油化学製品の製造が行われている。この熱分解により生成されるガスには、CO2及びH2Sといった酸性ガスが含まれている。これらは、腐食や触媒毒等の原因となるため、塩基性洗浄により除去されている。
また、上記の熱分解では、例えば、アセトアルデヒド等のカルボニル化合物等が形成される。このアセトアルデヒド等のカルボニル化合物は、塩基性存在下でアルドール縮合し、形成されたポリマーが炭化水素分解プロセスにおける汚れの原因物質の一つとして知られている。
このため、カルボニル化合物の重合を抑制して炭化水素分解プロセスの汚れを防止する方法が提案されている(例えば、特許文献1〜3)。
BACKGROUND ART Petrochemical products such as ethylene and propylene are produced by using hydrocarbons such as ethane, propane, butane, naphtha, light oil or a mixture thereof as a raw material and thermally decomposing them. The gas generated by this thermal decomposition contains acidic gases such as CO 2 and H 2 S. Since these cause corrosion and catalyst poisoning, they are removed by basic cleaning.
In the above thermal decomposition, for example, a carbonyl compound such as acetaldehyde is formed. This carbonyl compound such as acetaldehyde undergoes aldol condensation in the presence of a basic substance, and the formed polymer is known as one of the causative substances of soil in the hydrocarbon decomposition process.
For this reason, the method of suppressing the superposition | polymerization of a carbonyl compound and preventing the contamination | pollution | contamination of a hydrocarbon decomposition process is proposed (for example, patent documents 1-3).

特許文献1は、亜ジチオン酸塩等の無機塩と6−アミノカプロン酸とを用いて、炭化水素分解プロセス中の苛性アルカリ洗浄ユニットシステムの供給流に含まれる成分の重合を抑制及び堆積物を溶解する方法を開示する。
特許文献2は、α−アミノ酸等を用いて、炭化水素クラッキング工程の塩基性洗浄装置の操作におけるカルボニル化合物の重合を抑制する方法を開示する。
特許文献3は、ヒドロキシルアミンの存在下で炭化水素を塩基性洗浄することを開示する。
Patent Document 1 uses an inorganic salt such as dithionite and 6-aminocaproic acid to suppress polymerization of components contained in the feed stream of the caustic cleaning unit system during the hydrocarbon cracking process and dissolve deposits A method is disclosed.
Patent Document 2 discloses a method of suppressing polymerization of a carbonyl compound in an operation of a basic cleaning apparatus in a hydrocarbon cracking process using α-amino acid or the like.
U.S. Patent No. 6,057,031 discloses basic washing of hydrocarbons in the presence of hydroxylamine.

特表2005−530903号公報JP 2005-530903 A 特表2004−513213号公報JP-T-2004-513213 特開昭62−87530号公報JP-A-62-87530

そこで、本開示は、一又は複数の実施形態において、炭化水素分解プロセスの塩基性洗浄において生成されるカルボニル化合物の重合物を溶解可能な方法を提供する。   Accordingly, the present disclosure provides, in one or a plurality of embodiments, a method capable of dissolving a polymer of a carbonyl compound generated in a basic cleaning of a hydrocarbon cracking process.

本開示は、一又は複数の実施形態において、炭化水素分解プロセスの塩基性洗浄において生成されるカルボニル化合物の重合物を溶解する方法であって、前記重合物を、ヒドロキシルアミン又はその塩と接触させることを含む溶解方法に関する。   The present disclosure, in one or more embodiments, is a method for dissolving a polymer of a carbonyl compound produced in a basic washing of a hydrocarbon cracking process, wherein the polymer is contacted with hydroxylamine or a salt thereof. A dissolution method comprising:

本開示は、一又は複数の実施形態において、炭化水素分解プロセスの塩基性洗浄において生成されるカルボニル化合物の重合物を溶解するための組成物であって、有効成分としてヒドロキシルアミン又はその塩を含む、組成物に関する。   In one or a plurality of embodiments, the present disclosure is a composition for dissolving a polymer of a carbonyl compound generated in a basic washing of a hydrocarbon cracking process, and includes hydroxylamine or a salt thereof as an active ingredient , Relating to the composition.

本開示は、一又は複数の実施形態において、エチレン製造プラントにおける汚れ防止方法であって、前記エチレン製造プラントは、炭化水素分解プロセスの塩基性洗浄工程を含み、ヒドロキシルアミン又はその塩を、前記塩基性洗浄が行われる洗浄装置から排出される洗浄廃液に添加することを含む、汚れ防止方法に関する。   In one or a plurality of embodiments, the present disclosure is a method for preventing fouling in an ethylene production plant, the ethylene production plant including a basic cleaning step of a hydrocarbon cracking process, wherein hydroxylamine or a salt thereof is added to the base. The present invention relates to a method for preventing contamination, which includes adding to a cleaning waste liquid discharged from a cleaning apparatus in which sexual cleaning is performed.

本開示は、一又は複数の実施形態において、炭化水素分解プロセスの塩基性洗浄において生成されるカルボニル化合物の重合物を溶解できる。   In one or a plurality of embodiments, the present disclosure can dissolve a polymer of a carbonyl compound produced in a basic washing of a hydrocarbon cracking process.

図1は、エチレンプラントにおける塩基性洗浄及び廃液処理工程の一例を示す概略図である。FIG. 1 is a schematic view showing an example of a basic cleaning and waste liquid treatment process in an ethylene plant. 図2Aは、実機での確認試験の結果の一例を示すグラフであって、pH計電極のクリーニング回数の一例を示すグラフである。FIG. 2A is a graph showing an example of the result of a confirmation test with an actual machine, and is an example of the number of cleanings of the pH meter electrode. 図2Bは、実機での確認試験の結果の一例を示すグラフであって、堆積物(ポリマー)の堆積率を示すグラフである。FIG. 2B is a graph showing an example of a result of a confirmation test using an actual machine, and a graph showing a deposition rate of a deposit (polymer). 図2Cは、実機での確認試験の結果の一例を示すグラフであって、pH計電極のクリーニング回数を示すグラフである。FIG. 2C is a graph showing an example of a result of a confirmation test using an actual machine, and is a graph showing the number of times the pH meter electrode is cleaned.

図1に、エチレンプラントにおける塩基性洗浄及びそれにより排出される廃液の流れの一例を示す。図1に示すように、ナフサ又はエタン等の原料を熱分解することにより得られたガスは、洗浄塔1の下部から洗浄塔1に導入される(図1のa)。洗浄塔1に導入されたガスは、洗浄塔1内で苛性ソーダ等の塩基性洗浄液で酸性ガス(CO2及びH2S等)等の除去が行われ、洗浄塔1の上部からコンプレッサー等に排出される(図1のb)。一方、洗浄塔1の廃液は、洗浄塔1の下部から排出され、廃アルカリ沈降槽ドラム2やレッドオイルスキミングドラム3での処理を経てタンク4に回収される。その後、タワー5に供給され、生成されたガスはタワー5の上部から排出され、廃液はタワー5の下部から排出されてストレーナー6及びポンプを通じて沈降槽7に回収される。この工程において、洗浄塔1から排出される廃液に含まれるカルボニル化合物の重合物が、タンク4、タワー5、ストレーナー6、又は沈降槽7等に堆積することが問題となっている。 FIG. 1 shows an example of basic cleaning in an ethylene plant and the flow of waste liquid discharged thereby. As shown in FIG. 1, a gas obtained by pyrolyzing a raw material such as naphtha or ethane is introduced into the cleaning tower 1 from the lower part of the cleaning tower 1 (a in FIG. 1). The gas introduced into the cleaning tower 1 is removed in the cleaning tower 1 with acidic cleaning liquid such as caustic soda (CO 2 and H 2 S, etc.) and discharged from the upper part of the cleaning tower 1 to a compressor and the like. (B in FIG. 1). On the other hand, the waste liquid in the washing tower 1 is discharged from the lower part of the washing tower 1 and is collected in the tank 4 through the treatment in the waste alkali sedimentation tank drum 2 and the red oil skimming drum 3. Thereafter, the gas is supplied to the tower 5, and the generated gas is discharged from the upper part of the tower 5, and the waste liquid is discharged from the lower part of the tower 5 and collected in the sedimentation tank 7 through the strainer 6 and the pump. In this step, there is a problem that the polymer of the carbonyl compound contained in the waste liquid discharged from the cleaning tower 1 is accumulated in the tank 4, the tower 5, the strainer 6, the sedimentation tank 7, or the like.

本開示は、ヒドロキシルアミン又はその塩を用いることによって、炭化水素分解プロセスの塩基性洗浄において生成されるカルボニル化合物の重合物を溶解できる、という知見に基づく。本開示は、塩基性洗浄により排出される廃液にヒドロキシルアミン又はその塩を添加することによって、炭化水素分解プロセスの塩基性洗浄において生成されるカルボニル化合物の重合物を溶解でき、それらの堆積を抑制又は防止できる、という知見に基づく。   The present disclosure is based on the finding that by using hydroxylamine or a salt thereof, a polymer of the carbonyl compound produced in the basic washing of the hydrocarbon cracking process can be dissolved. In this disclosure, by adding hydroxylamine or a salt thereof to the waste liquid discharged from the basic cleaning, the polymer of the carbonyl compound generated in the basic cleaning of the hydrocarbon decomposition process can be dissolved, and their deposition is suppressed. Or based on the knowledge that it can be prevented.

本開示によれば、一又は複数の実施形態において、ヒドロキシルアミン又はその塩を用いることによって、炭化水素分解プロセスの塩基性洗浄において生成されるカルボニル化合物の重合物を、溶解できるという効果を奏しうる。さらには、一又は複数の実施形態において、本開示によれば、炭化水素分解プロセスの塩基性洗浄において生成されるカルボニル化合物の重合物を溶解できることから、塩基性洗浄においてカルボニル化合物の重合物が生成された場合であっても、エチレン製造プラントにおける汚れの抑制又は防止を効率よく行うことができるという効果を奏しうる。   According to the present disclosure, in one or a plurality of embodiments, by using hydroxylamine or a salt thereof, the polymer of the carbonyl compound generated in the basic washing of the hydrocarbon decomposition process can be dissolved. . Furthermore, in one or a plurality of embodiments, according to the present disclosure, a polymer of a carbonyl compound generated in a basic cleaning of a hydrocarbon cracking process can be dissolved, and thus a polymer of a carbonyl compound is generated in a basic cleaning. Even in such a case, it is possible to effectively suppress or prevent soiling in the ethylene production plant.

[カルボニル化合物の重合物の溶解方法]
本開示は、一又は複数の実施形態において、炭化水素分解プロセスの塩基性洗浄において生成されるカルボニル化合物の重合物を溶解する方法であって、前記重合物を、ヒドロキシルアミン又はその塩と接触させることを含む溶解方法に関する。
[Method of dissolving polymer of carbonyl compound]
The present disclosure, in one or more embodiments, is a method for dissolving a polymer of a carbonyl compound produced in a basic washing of a hydrocarbon cracking process, wherein the polymer is contacted with hydroxylamine or a salt thereof. A dissolution method comprising:

本開示において、炭化水素分解プロセスとしては、一又は複数の実施形態において、ナフサクラッキング、エタンクラッキング等が挙げられる。本開示において、炭化水素分解プロセスの原料としては、一又は複数の実施形態において、ナフサ又はエタン等が挙げられる。   In the present disclosure, examples of the hydrocarbon cracking process include naphtha cracking, etantac racking, and the like in one or a plurality of embodiments. In the present disclosure, the raw material for the hydrocarbon cracking process includes naphtha or ethane in one or more embodiments.

本開示において、炭化水素分解プロセスの塩基性洗浄において生成されるカルボニル化合物の重合物としては、一又は複数の実施形態において、アセトアルデヒドのアルドール縮合により生じるアルドールポリマー、又はレッドオイルと呼ばれる縮合ポリマーが挙げられる。   In the present disclosure, the polymer of the carbonyl compound generated in the basic washing of the hydrocarbon cracking process includes, in one or more embodiments, an aldol polymer generated by aldol condensation of acetaldehyde or a condensation polymer called red oil. It is done.

本開示において、塩基性洗浄塔としては、一又は複数の実施形態において、苛性ソーダ洗浄塔、アミン洗浄塔等が挙げられる。   In the present disclosure, examples of the basic washing tower include a caustic soda washing tower and an amine washing tower in one or a plurality of embodiments.

本開示は、カルボニル化合物の重合物を効率よく溶解できる点から、一又は複数の実施形態において、ヒドロキシルアミン又はその塩を、塩基性洗浄が行われる洗浄装置から排出される洗浄廃液に添加することを含む。本開示は、一又は複数の実施形態において、塩基性洗浄塔のボトムよりも下流にヒドロキシルアミン又はその塩を導入することを含む。   In one or a plurality of embodiments, the present disclosure adds hydroxylamine or a salt thereof to a cleaning waste liquid discharged from a cleaning apparatus in which basic cleaning is performed, from the viewpoint that a polymer of a carbonyl compound can be efficiently dissolved. including. In one or more embodiments, the present disclosure includes introducing hydroxylamine or a salt thereof downstream from the bottom of the basic wash tower.

ヒドロキシルアミンの塩としては、一又は複数の実施形態において、リン酸塩、硫酸塩、亜硫酸塩、塩酸塩、硝酸塩、酢酸塩及びプロピオン酸塩等が挙げられる。アルドールポリマーの溶解性の点から、ヒドロキシルアミンの塩としては、硫酸塩及び塩酸塩が好ましく、より好ましくはヒドロキシルアミンの硫酸塩である。本開示は、一又は複数の実施形態において、硫酸ヒドロキシルアミン、塩酸ヒドロキシルアミン、及びヒドロキシルアミン並びにこれらの組み合わせからなる群から選択される少なくとも一つを有効成分として使用することを含む。   Examples of the hydroxylamine salt include phosphate, sulfate, sulfite, hydrochloride, nitrate, acetate, and propionate in one or more embodiments. From the viewpoint of the solubility of the aldol polymer, the hydroxylamine salt is preferably sulfate or hydrochloride, more preferably hydroxylamine sulfate. In one or more embodiments, the present disclosure includes using as an active ingredient at least one selected from the group consisting of hydroxylamine sulfate, hydroxylamine hydrochloride, and hydroxylamine, and combinations thereof.

本開示において、ヒドロキシルアミン又はその塩の添加濃度は特に限定されず、アルドールポリマーを溶解除去し炭化水素分解プロセスにおける汚れを効率的に抑制又は防止する点から、塩基性洗浄装置から排出される洗浄廃液量に対して、1mg/L以上、好ましくは2mg/L以上であり、アルドールポリマーの溶解に要する経済性の点から、100mg/L以下、好ましくは50mg/L以下である。   In the present disclosure, the concentration of hydroxylamine or a salt thereof added is not particularly limited, and cleaning discharged from the basic cleaning device is effective in that the aldol polymer is dissolved and removed to effectively suppress or prevent soiling in the hydrocarbon decomposition process. The amount is 1 mg / L or more, preferably 2 mg / L or more with respect to the amount of waste liquid, and is 100 mg / L or less, preferably 50 mg / L or less, from the viewpoint of economy required for dissolving the aldol polymer.

本開示において、ヒドロキシルアミン又はその塩の添加頻度は特に限定されず、汚れの程度に応じて添加回数及び添加時間は適時選択できる。ヒドロキシルアミン又はその塩の添加は、一又は複数の実施形態において、連続添加であってもよいし、断続的に添加してもよく、添加回数及び添加時間は適時選択でき、アルドールポリマーを溶解除去し炭化水素分解プロセスにおける汚れを効率的に抑制又は防止できる程度であればよい。   In the present disclosure, the frequency of addition of hydroxylamine or a salt thereof is not particularly limited, and the number of additions and the addition time can be appropriately selected according to the degree of soiling. In one or a plurality of embodiments, the addition of hydroxylamine or a salt thereof may be added continuously or intermittently, and the number of additions and the addition time can be selected as appropriate, and the aldol polymer is dissolved and removed. However, it is sufficient that the contamination in the hydrocarbon cracking process can be efficiently suppressed or prevented.

本開示において、ヒドロキシルアミン又はその塩は、一又は複数の実施形態において、固体、粉体又は水溶液の形態で使用することができる。水溶液として使用する場合、水溶液中におけるヒドロキシルアミン又はその塩の濃度は、特に限定されるものではないが、組成物の安全性、安定性、コスト及び/又は添加のしやすさの点から、5重量%以上又は10重量%以上含み、50重量%以下又は40重量%以下が好ましい。   In the present disclosure, hydroxylamine or a salt thereof can be used in the form of a solid, powder or aqueous solution in one or more embodiments. When used as an aqueous solution, the concentration of hydroxylamine or a salt thereof in the aqueous solution is not particularly limited. From the viewpoint of safety of the composition, stability, cost, and / or ease of addition, 5 It contains 50% by weight or less or 40% by weight or less.

[カルボニル化合物の重合物を溶解するための組成物]
本開示は、一又は複数の実施形態において、炭化水素分解プロセスの塩基性洗浄において生成されるカルボニル化合物の重合物を溶解するための組成物であって、有効成分としてヒドロキシルアミン又はその塩を含む組成物に関する。本開示の組成物によれば、一又は複数の実施形態において、炭化水素分解プロセスの塩基性洗浄において生成されるカルボニル化合物の重合物を効率よく溶解することができ、好ましくはエチレン製造プラントにおける汚れを効率よく防止することができる。本開示の組成物は、一又は複数の実施形態において、本開示の溶解方法に用いることができる。
[Composition for dissolving polymer of carbonyl compound]
In one or a plurality of embodiments, the present disclosure is a composition for dissolving a polymer of a carbonyl compound generated in a basic washing of a hydrocarbon cracking process, and includes hydroxylamine or a salt thereof as an active ingredient Relates to the composition. According to the composition of the present disclosure, in one or a plurality of embodiments, it is possible to efficiently dissolve a polymer of a carbonyl compound produced in a basic cleaning of a hydrocarbon cracking process, and preferably a fouling in an ethylene production plant. Can be efficiently prevented. The composition of this indication can be used for the dissolution method of this indication in one or some embodiment.

本開示の組成物において、ヒドロキシルアミン又はその塩は、上述のとおりである。本開示の組成物は、一又は複数の実施形態において、有効成分として、硫酸ヒドロキシルアミン、塩酸ヒドロキシルアミン、及びヒドロキシルアミン並びにこれらの組み合わせからなる群から選択される少なくとも一つを含有する。   In the composition of the present disclosure, the hydroxylamine or a salt thereof is as described above. In one or more embodiments, the composition of the present disclosure contains, as an active ingredient, at least one selected from the group consisting of hydroxylamine sulfate, hydroxylamine hydrochloride, and hydroxylamine and combinations thereof.

本開示の組成物は、一又は複数の実施形態において、固体、粉体又は水溶液の形態が挙げられる。組成物が固体または粉体の場合は、予め溶解して水溶液としてもよいし、そのまま添加してもよい。ヒドロキシルアミン又はその塩の水への溶解度に応じた濃度で水溶液の形態で添加することができるが、組成物の安全性、安定性、コスト及び/又は添加のしやすさの点から、5重量%以上又は10重量%以上含み、50重量%以下又は40重量%以下含むのが好ましいが、特に限定されるものではない。   The composition of the present disclosure may be in the form of a solid, powder or aqueous solution in one or more embodiments. When the composition is solid or powder, it may be dissolved in advance to form an aqueous solution, or may be added as it is. Hydroxylamine or a salt thereof can be added in the form of an aqueous solution at a concentration depending on the solubility in water, but 5% by weight from the viewpoint of the safety, stability, cost and / or ease of addition of the composition % Or 10% by weight or more, preferably 50% by weight or less or 40% by weight or less, but is not particularly limited.

[汚れ防止方法]
本開示は、一又は複数の実施形態において、エチレン製造プラントにおける汚れ防止方法であって、エチレン製造プラントは、炭化水素分解プロセスの塩基性洗浄工程を含み、ヒドロキシルアミン又はその塩を、前記塩基性洗浄が行われる洗浄装置から排出される洗浄廃液に添加することを含む汚れ防止方法に関する。
本開示の汚れ防止方法は、一又は複数の実施形態において、本開示の溶解方法を行うことを含む。
[Stain prevention method]
In one or a plurality of embodiments, the present disclosure is a method for preventing fouling in an ethylene production plant, the ethylene production plant including a basic cleaning step of a hydrocarbon cracking process, wherein hydroxylamine or a salt thereof is added to the basic production step. The present invention relates to a stain prevention method including adding to a cleaning waste liquid discharged from a cleaning apparatus in which cleaning is performed.
In one or a plurality of embodiments, the dirt prevention method of the present disclosure includes performing the dissolution method of the present disclosure.

本開示は、以下の、一又は複数の実施形態に関しうる;
〔1〕 炭化水素分解プロセスの塩基性洗浄において生成されるカルボニル化合物の重合物を溶解する方法であって、
前記重合物を、ヒドロキシルアミン又はその塩と接触させることを含む、溶解方法。
〔2〕 前記ヒドロキシルアミン又はその塩を、前記塩基性洗浄が行われる洗浄装置から排出される洗浄廃液に添加することを含む、〔1〕記載の溶解方法。
〔3〕 前記ヒドロキシルアミン又はその塩は、硫酸ヒドロキシルアミン、塩酸ヒドロキシルアミン、及びヒドロキシルアミン並びにこれらの組み合わせからなる群から選択される、〔1〕又は〔2〕に記載の溶解方法。
〔4〕 炭化水素分解プロセスの塩基性洗浄において生成されるカルボニル化合物の重合物を溶解するための組成物であって、
有効成分としてヒドロキシルアミン又はその塩を含む、組成物。
〔5〕 エチレン製造プラントにおける汚れ防止方法であって、
前記エチレン製造プラントは、炭化水素分解プロセスの塩基性洗浄工程を含み、
ヒドロキシルアミン又はその塩を、前記塩基性洗浄が行われる洗浄装置から排出される洗浄廃液に添加することを含む、汚れ防止方法。
The present disclosure may relate to one or more of the following embodiments;
[1] A method for dissolving a polymer of a carbonyl compound produced in basic washing of a hydrocarbon cracking process,
A dissolution method comprising contacting the polymer with hydroxylamine or a salt thereof.
[2] The dissolution method according to [1], comprising adding the hydroxylamine or a salt thereof to a cleaning waste liquid discharged from a cleaning apparatus in which the basic cleaning is performed.
[3] The dissolution method according to [1] or [2], wherein the hydroxylamine or a salt thereof is selected from the group consisting of hydroxylamine sulfate, hydroxylamine hydrochloride, hydroxylamine, and combinations thereof.
[4] A composition for dissolving a polymer of a carbonyl compound produced in basic washing of a hydrocarbon cracking process,
A composition comprising hydroxylamine or a salt thereof as an active ingredient.
[5] A method for preventing contamination in an ethylene production plant,
The ethylene production plant includes a basic cleaning step of a hydrocarbon cracking process;
A method for preventing soiling, comprising adding hydroxylamine or a salt thereof to a cleaning waste liquid discharged from a cleaning apparatus in which the basic cleaning is performed.

以下、実施例を用いて本開示をさらに説明する。ただし、本開示は以下の実施例に限定して解釈されない。   Hereinafter, the present disclosure will be further described using examples. However, the present disclosure is not construed as being limited to the following examples.

[アルドール縮合物溶解効果の確認]
ヒドロキシルアミン又はその塩のアルドール縮合物溶解効果を明確にするため卓上試験にてアルドールポリマーを析出させた試験液を調製しそれを用いて評価を行った。まず、5規定の水酸化ナトリウム水溶液30mLをビーカーに採取し、純水45mLを加えて撹拌した。ついで撹拌しながら、酢酸ビニルを5g加え、発熱が終了するまで撹拌することでアルドール縮合を生じせしめアルドールポリマーを含む試験液Aを調製した。
別途、下記表1に示す薬剤を表1に記載の添加量となるように10mLフタ付スピッツに加え、純水5mLに溶解し、ついで試験液Aを5mL分注して激しく10回手振りした後、10分間静置した。その後、濁度(800nm)の測定を行った。その結果を下記表1に示す。
Blankは、薬剤を含有しない純水5mLに試験液A5mLを分注し、上記と同様の測定を行った。
[Confirmation of dissolution effect of aldol condensate]
In order to clarify the effect of dissolving an aldol condensate of hydroxylamine or a salt thereof, a test solution in which an aldol polymer was precipitated was prepared by a desktop test and evaluated using the test solution. First, 30 mL of a 5N aqueous sodium hydroxide solution was collected in a beaker, and 45 mL of pure water was added and stirred. Next, 5 g of vinyl acetate was added while stirring, and stirring was continued until the exotherm was completed, thereby causing aldol condensation to prepare Test Solution A containing an aldol polymer.
Separately, the chemicals shown in Table 1 below were added to Spitz with a 10 mL lid so as to have the addition amount shown in Table 1, dissolved in 5 mL of pure water, and then 5 mL of Test Solution A was dispensed and shaken vigorously 10 times. Allowed to stand for 10 minutes. Thereafter, turbidity (800 nm) was measured. The results are shown in Table 1 below.
Blank dispensed 5 mL of test solution A into 5 mL of pure water containing no drug, and performed the same measurement as above.

Figure 0006464377
Figure 0006464377

表1に示すように、硫酸ヒドロキシルアミン、塩酸ヒドロキシルアミン又はヒドロキシルアミンを用いることにより、亜ジチオン酸ナトリウムと6−アミノカプロン酸との混合物、グリシンナトリウム、又はジエチルヒドロキシルアミンを使用した場合と比較して、試験液中のアルドールポリマーを溶解することができた。また、目視により外観の観察を行ったところ、比較例はいずれも白濁していたのに対し、実施例ではいずれもアルドールポリマーを溶解していることが確認できた。   As shown in Table 1, by using hydroxylamine sulfate, hydroxylamine hydrochloride or hydroxylamine, compared to using a mixture of sodium dithionite and 6-aminocaproic acid, sodium glycine, or diethylhydroxylamine. The aldol polymer in the test solution could be dissolved. Further, when the appearance was visually observed, it was confirmed that all the comparative examples were clouded, whereas in the examples, the aldol polymer was dissolved.

[実機での確認試験]
図1に示すエチレンプラントの苛性ソーダ洗浄塔1と、苛性ソーダ洗浄塔1の塔底部から排出される洗浄廃液を回収するタンク2とを接続する部分(図1の矢印Xで示す位置)に、硫酸ヒドロキシルアミン水溶液を、洗浄廃液量に対して3.3mg/L連続添加した場合と、硫酸ヒドロキシルアミン水溶液を添加しない場合を稼働日数100日において比較した。その結果を図2A及びBに示す。図2Aは、図1のAで示す位置に配置されたポリマーが付着しやすいpH計電極のクリーニング回数を示すグラフであり、図2Bは、図1の沈降槽7の堆積物(ポリマー)の堆積率を示すグラフである。なお、ポリマー堆積率は、ポリマーが堆積すると外気温の影響を受けてタンクの表面温度が低下する性質を利用して表面温度計による計測により求めた。また、堆積物が、カルボニル化合物の重合物であることは、赤外分光法及び800度下での灼熱減量測定等の定性試験により確認した。
一方、硫酸ヒドロキシルアミン水溶液が無添加の状態から洗浄廃液量に対して20日間1.5mg/L連続添加したあと15日間無添加の状態にし、その後は3.3mg/L連続添加した確認試験を行った。pH計電極のクリーニング回数のみで評価し、その結果を図2Cに示す。
[Confirmation test with actual machine]
Hydroxyl sulfate is connected to a portion (position indicated by arrow X in FIG. 1) connecting the caustic soda washing tower 1 of the ethylene plant shown in FIG. 1 and a tank 2 for collecting the washing waste liquid discharged from the bottom of the caustic soda washing tower 1. The case where the aqueous amine solution was continuously added to the washing waste liquid amount of 3.3 mg / L and the case where the hydroxylamine sulfate aqueous solution was not added were compared in 100 working days. The results are shown in FIGS. 2A and 2B. FIG. 2A is a graph showing the number of cleanings of the pH meter electrode to which the polymer arranged at the position indicated by A in FIG. 1 is likely to adhere, and FIG. 2B is the deposition of the deposit (polymer) in the settling tank 7 in FIG. It is a graph which shows a rate. The polymer deposition rate was determined by measurement with a surface thermometer utilizing the property that the surface temperature of the tank decreases due to the influence of the outside air temperature when the polymer is deposited. Further, it was confirmed by a qualitative test such as infrared spectroscopy and measurement of loss of ignition under 800 ° C. that the deposit was a polymer of a carbonyl compound.
On the other hand, a confirmation test was conducted in which 1.5 mg / L was continuously added for 20 days from the state in which the hydroxylamine sulfate aqueous solution was not added to the washing waste liquid amount, then was added for 15 days, and then 3.3 mg / L was continuously added. went. Evaluation was made only by the number of cleanings of the pH meter electrode, and the result is shown in FIG. 2C.

図2A及びBに示すように、硫酸ヒドロキシルアミンの添加後は、pH計の電極に付着するポリマー量が低減され、クリーニング回数を1週間あたり56回から4回へと大幅に低減できたとともに、ポリマーの堆積率も大幅に低減された。
また、図2Cに示すように、添加濃度を変化させた場合も、硫酸ヒドロキシルアミン無添加時に毎日8回程度であったクリーニング回数が、1.5mg/L連続添加してしばらくすると4回程度に半減した。その後添加を15日間やめてもクリーニング回数が増えることはなかった。その後3.3mg/L連続添加にするとクリーニング回数が2回程度に減った上にクリーニングせずにすむ日もあった。これは、系内に堆積していたポリマーが硫酸ヒドロキシルアミンの溶解効果によって徐々に溶け出したために添加のタイミングとクリーニング回数の減少のタイミングにタイムラグが生じたもの考えられ、硫酸ヒドロキシルアミンの溶解効果を支持する結果である。
As shown in FIGS. 2A and 2B, after adding hydroxylamine sulfate, the amount of polymer adhering to the electrode of the pH meter was reduced, and the number of cleanings was greatly reduced from 56 to 4 times per week. The polymer deposition rate was also greatly reduced.
Further, as shown in FIG. 2C, even when the addition concentration was changed, the cleaning frequency, which was about 8 times a day when hydroxylamine sulfate was not added, became about 4 times after 1.5 mg / L was continuously added. Halved. Thereafter, the number of cleanings did not increase even after the addition was stopped for 15 days. Thereafter, when 3.3 mg / L was continuously added, the number of cleanings was reduced to about 2 times, and there was a day when cleaning was not necessary. This is probably because the polymer deposited in the system gradually dissolved due to the dissolution effect of hydroxylamine sulfate, which caused a time lag between the timing of addition and the decrease in the number of cleanings. This is a result of supporting.

Claims (4)

炭化水素分解プロセスの塩基性洗浄において生成されるカルボニル化合物の重合物を溶解する方法であって、
ヒドロキシルアミン又はその塩を、前記塩基性洗浄が行われる洗浄装置から排出される洗浄廃液に添加することにより、前記重合物を、ヒドロキシルアミン又はその塩と接触させることを含む、溶解方法。
A method for dissolving a polymer of a carbonyl compound produced in a basic washing of a hydrocarbon cracking process, comprising:
A dissolution method comprising contacting the polymer with hydroxylamine or a salt thereof by adding hydroxylamine or a salt thereof to a washing waste liquid discharged from a washing apparatus in which the basic washing is performed .
前記ヒドロキシルアミン又はその塩は、硫酸ヒドロキシルアミン、塩酸ヒドロキシルアミン、及びヒドロキシルアミン並びにこれらの組み合わせからなる群から選択される、請求項記載の溶解方法。 The hydroxylamine or its salt, hydroxylamine sulfate, hydroxylamine hydrochloride, and is selected from hydroxylamine and combinations thereof, dissolution process of claim 1. 炭化水素分解プロセスの塩基性洗浄において生成されるカルボニル化合物の重合物を溶解するための組成物であって、
有効成分としてヒドロキシルアミン又はその塩を含む、組成物。
A composition for dissolving a polymer of a carbonyl compound produced in basic washing of a hydrocarbon cracking process,
A composition comprising hydroxylamine or a salt thereof as an active ingredient.
エチレン製造プラントにおける汚れ防止方法であって、
前記エチレン製造プラントは、炭化水素分解プロセスの塩基性洗浄工程を含み、
ヒドロキシルアミン又はその塩を、前記塩基性洗浄が行われる洗浄装置から排出される洗浄廃液に添加することを含む、汚れ防止方法。
A method for preventing contamination in an ethylene production plant,
The ethylene production plant includes a basic cleaning step of a hydrocarbon cracking process;
A method for preventing soiling, comprising adding hydroxylamine or a salt thereof to a cleaning waste liquid discharged from a cleaning apparatus in which the basic cleaning is performed.
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