JPH0460131B2 - - Google Patents
Info
- Publication number
- JPH0460131B2 JPH0460131B2 JP7932484A JP7932484A JPH0460131B2 JP H0460131 B2 JPH0460131 B2 JP H0460131B2 JP 7932484 A JP7932484 A JP 7932484A JP 7932484 A JP7932484 A JP 7932484A JP H0460131 B2 JPH0460131 B2 JP H0460131B2
- Authority
- JP
- Japan
- Prior art keywords
- reciprocating compressor
- ethylene
- fluid
- compressor according
- reactor
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 claims description 29
- 239000005977 Ethylene Substances 0.000 claims description 29
- 239000012530 fluid Substances 0.000 claims description 27
- 238000007789 sealing Methods 0.000 claims description 16
- 238000006116 polymerization reaction Methods 0.000 claims description 14
- 239000000463 material Substances 0.000 claims description 13
- 229910052751 metal Inorganic materials 0.000 claims description 12
- 239000002184 metal Substances 0.000 claims description 12
- 239000002245 particle Substances 0.000 claims description 9
- 239000003054 catalyst Substances 0.000 claims description 8
- 239000011230 binding agent Substances 0.000 claims description 7
- 239000004605 External Lubricant Substances 0.000 claims description 6
- 239000000203 mixture Substances 0.000 claims description 6
- 229920000642 polymer Polymers 0.000 claims description 6
- 239000004711 α-olefin Substances 0.000 claims description 6
- 150000001875 compounds Chemical class 0.000 claims description 5
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 claims description 4
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims description 4
- 239000013078 crystal Substances 0.000 claims description 4
- 239000010936 titanium Substances 0.000 claims description 4
- 229910052719 titanium Inorganic materials 0.000 claims description 4
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 claims description 3
- 229910052782 aluminium Inorganic materials 0.000 claims description 3
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 3
- 229910052804 chromium Inorganic materials 0.000 claims description 3
- 239000011651 chromium Substances 0.000 claims description 3
- 239000001257 hydrogen Substances 0.000 claims description 3
- 229910052739 hydrogen Inorganic materials 0.000 claims description 3
- 230000008018 melting Effects 0.000 claims description 3
- 238000002844 melting Methods 0.000 claims description 3
- 150000002739 metals Chemical class 0.000 claims description 3
- 229910045601 alloy Inorganic materials 0.000 claims description 2
- 239000000956 alloy Substances 0.000 claims description 2
- 239000010941 cobalt Substances 0.000 claims description 2
- 229910017052 cobalt Inorganic materials 0.000 claims description 2
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 claims description 2
- 150000001247 metal acetylides Chemical class 0.000 claims description 2
- 229910052759 nickel Inorganic materials 0.000 claims description 2
- 150000004767 nitrides Chemical class 0.000 claims description 2
- 229930195734 saturated hydrocarbon Natural products 0.000 claims description 2
- 239000002904 solvent Substances 0.000 claims description 2
- WFKWXMTUELFFGS-UHFFFAOYSA-N tungsten Chemical compound [W] WFKWXMTUELFFGS-UHFFFAOYSA-N 0.000 claims description 2
- 229910052721 tungsten Inorganic materials 0.000 claims description 2
- 239000010937 tungsten Substances 0.000 claims description 2
- 125000004435 hydrogen atom Chemical class [H]* 0.000 claims 1
- 238000000034 method Methods 0.000 description 5
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 4
- 238000007334 copolymerization reaction Methods 0.000 description 4
- -1 propane Natural products 0.000 description 4
- 239000000178 monomer Substances 0.000 description 3
- VXNZUUAINFGPBY-UHFFFAOYSA-N 1-Butene Chemical compound CCC=C VXNZUUAINFGPBY-UHFFFAOYSA-N 0.000 description 2
- 229910000906 Bronze Inorganic materials 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 2
- 239000012190 activator Substances 0.000 description 2
- 125000005376 alkyl siloxane group Chemical group 0.000 description 2
- VSCWAEJMTAWNJL-UHFFFAOYSA-K aluminium trichloride Chemical compound Cl[Al](Cl)Cl VSCWAEJMTAWNJL-UHFFFAOYSA-K 0.000 description 2
- 239000010974 bronze Substances 0.000 description 2
- 239000001273 butane Substances 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- KUNSUQLRTQLHQQ-UHFFFAOYSA-N copper tin Chemical compound [Cu].[Sn] KUNSUQLRTQLHQQ-UHFFFAOYSA-N 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- IJDNQMDRQITEOD-UHFFFAOYSA-N n-butane Chemical compound CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 description 2
- OFBQJSOFQDEBGM-UHFFFAOYSA-N n-pentane Natural products CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 description 2
- 238000012856 packing Methods 0.000 description 2
- 239000001294 propane Substances 0.000 description 2
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 2
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 229910052723 transition metal Inorganic materials 0.000 description 2
- 150000003624 transition metals Chemical class 0.000 description 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 description 1
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- 229910001018 Cast iron Inorganic materials 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 description 1
- QCWXUUIWCKQGHC-UHFFFAOYSA-N Zirconium Chemical compound [Zr] QCWXUUIWCKQGHC-UHFFFAOYSA-N 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 150000001336 alkenes Chemical class 0.000 description 1
- AZDRQVAHHNSJOQ-UHFFFAOYSA-N alumane Chemical class [AlH3] AZDRQVAHHNSJOQ-UHFFFAOYSA-N 0.000 description 1
- 150000001412 amines Chemical class 0.000 description 1
- 125000003118 aryl group Chemical group 0.000 description 1
- 125000001797 benzyl group Chemical group [H]C1=C([H])C([H])=C(C([H])=C1[H])C([H])([H])* 0.000 description 1
- 239000008139 complexing agent Substances 0.000 description 1
- 229920001577 copolymer Polymers 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 150000001993 dienes Chemical class 0.000 description 1
- 150000002170 ethers Chemical class 0.000 description 1
- 230000005496 eutectics Effects 0.000 description 1
- 239000001307 helium Substances 0.000 description 1
- 229910052734 helium Inorganic materials 0.000 description 1
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 description 1
- 150000004678 hydrides Chemical class 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 239000003999 initiator Substances 0.000 description 1
- 239000000314 lubricant Substances 0.000 description 1
- 238000005461 lubrication Methods 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- 230000003287 optical effect Effects 0.000 description 1
- 150000002902 organometallic compounds Chemical class 0.000 description 1
- 230000000737 periodic effect Effects 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 230000000379 polymerizing effect Effects 0.000 description 1
- 150000003254 radicals Chemical class 0.000 description 1
- 239000011541 reaction mixture Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 229920001897 terpolymer Polymers 0.000 description 1
- UONOETXJSWQNOL-UHFFFAOYSA-N tungsten carbide Chemical compound [W+]#[C-] UONOETXJSWQNOL-UHFFFAOYSA-N 0.000 description 1
- 229910052720 vanadium Inorganic materials 0.000 description 1
- GPPXJZIENCGNKB-UHFFFAOYSA-N vanadium Chemical compound [V]#[V] GPPXJZIENCGNKB-UHFFFAOYSA-N 0.000 description 1
- 229910052726 zirconium Inorganic materials 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04B—POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
- F04B39/00—Component parts, details, or accessories, of pumps or pumping systems specially adapted for elastic fluids, not otherwise provided for in, or of interest apart from, groups F04B25/00 - F04B37/00
- F04B39/04—Measures to avoid lubricant contaminating the pumped fluid
- F04B39/041—Measures to avoid lubricant contaminating the pumped fluid sealing for a reciprocating rod
- F04B39/042—Measures to avoid lubricant contaminating the pumped fluid sealing for a reciprocating rod sealing being provided on the piston
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04B—POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
- F04B53/00—Component parts, details or accessories not provided for in, or of interest apart from, groups F04B1/00 - F04B23/00 or F04B39/00 - F04B47/00
- F04B53/14—Pistons, piston-rods or piston-rod connections
- F04B53/143—Sealing provided on the piston
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F16—ENGINEERING ELEMENTS AND UNITS; GENERAL MEASURES FOR PRODUCING AND MAINTAINING EFFECTIVE FUNCTIONING OF MACHINES OR INSTALLATIONS; THERMAL INSULATION IN GENERAL
- F16J—PISTONS; CYLINDERS; SEALINGS
- F16J9/00—Piston-rings, e.g. non-metallic piston-rings, seats therefor; Ring sealings of similar construction
- F16J9/26—Piston-rings, e.g. non-metallic piston-rings, seats therefor; Ring sealings of similar construction characterised by the use of particular materials
Landscapes
- Engineering & Computer Science (AREA)
- General Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Compressor (AREA)
- Polymerisation Methods In General (AREA)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
- Compressors, Vaccum Pumps And Other Relevant Systems (AREA)
Description
【発明の詳細な説明】
産業上の利用分野
本発明はエチレンの重合プロセス、特に、エチ
レンとα−オレフインとの共重合プロセスで用い
られる流体を極めて高い圧力に圧縮するのに用い
られる往復圧縮機に関するものである。DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention relates to a reciprocating compressor used to compress fluids used in ethylene polymerization processes, particularly in ethylene and α-olefin copolymerization processes, to extremely high pressures. It is related to.
従来の技術
従来を150バール以上の圧力に圧縮するには一
段に1段式または多段式の往復圧縮機が用いられ
る。この往復圧縮機のシリンダの内部にはピスト
ンプランジヤーまたはシリンダジヤケツトが収容
され、密封エレメントが用いられる。ピストンプ
ランジヤーの場合には密封エレメントは複数の部
材よりなる少なくとも1つの静止パツキンであ
り、シリンダジヤケツトの場合には密封エレメン
トはピストンと一体の少なくとも1つの可動セグ
メントである。静止パツキンの場合には静止パツ
キンとピストンプランジヤーとの間で動的シール
が行われ、可動セグメントの場合にはシリンダジ
ヤケツトと可動セグメントとの間で動的シールが
行われる。PRIOR ART Conventionally, single-stage or multi-stage reciprocating compressors are used to compress pressures above 150 bar. Inside the cylinder of this reciprocating compressor, a piston plunger or cylinder jacket is housed and a sealing element is used. In the case of a piston plunger, the sealing element is at least one stationary seal made of several parts; in the case of a cylinder jacket, the sealing element is at least one movable segment integral with the piston. In the case of a stationary packing, a dynamic seal is provided between the stationary packing and the piston plunger, and in the case of a moving segment, a dynamic seal is provided between the cylinder jacket and the moving segment.
本発明は、下記3つの条件の少なくとも1つに
当てはまるような流体に特に適している:
(1) 痕跡量の摩耗性粒子を含む流体
(2) 自己潤滑性が無く且つ外部潤滑剤の添加はで
きないプロセスに用いられる流体
(3) 自己潤滑性が無く且つ外部潤滑剤の添加はで
きるが潤滑剤の溶媒となる流体
被圧縮流体が上記3つの条件に全く当てはまら
ない場合、特に、自己潤滑性がありおよび/また
は痕跡の摩耗性磨粒子を含まない場合、および/
または動的密封エレメントと接触した表面が潤滑
性がある場合には、圧縮機は7000時間以上安定に
運転でき、圧縮機の構成部品の材料に特別な注意
を払う必要はない。 The present invention is particularly suitable for fluids in which at least one of the following three conditions apply: (1) fluids that contain trace amounts of abrasive particles; (2) fluids that are not self-lubricating and the addition of external lubricants is (3) A fluid that does not have self-lubricating properties and can be used as a solvent for the lubricant, although an external lubricant can be added.If the fluid to be compressed does not meet any of the above three conditions, especially if the fluid does not have self-lubricating properties. with and/or without traces of abrasive particles; and/or
Alternatively, if the surfaces in contact with the dynamic sealing element are lubricated, the compressor can operate stably for more than 7000 hours without requiring special attention to the materials of the compressor components.
例えばフランス特許第1584529号、第2025887
号、第2099267号および第2313399号に記載されて
いるように、エチレンまたはエチレンと極性コモ
ノマーとの混合物を150〜3000バールまで加圧し
て遊離ラジカル開始剤の存在下で高温度で重合す
るプロセスで使用される往復圧縮機では、一般
に、ピストンプランジヤーまたはシリンダジヤケ
ツトが処理鋼、鋳物または炭化タングステン等の
金属炭化物で作られ、密封エレメントは錫9%、
燐0.3〜1%、残部が銅である青銅、例えばUE9P
青銅で作られる。これらの材料が使用できるの
は、被圧縮流体のエチレン中に痕跡の研磨性磨粒
子が含まれていない場合である。 For example French patent no. 1584529, no. 2025887
No. 2099267 and No. 2313399, a process in which ethylene or a mixture of ethylene and a polar comonomer is polymerized at high temperatures in the presence of free radical initiators under pressure up to 150-3000 bar. In the reciprocating compressors used, the piston plunger or cylinder jacket is generally made of treated steel, cast iron or a metal carbide such as tungsten carbide, and the sealing element is made of 9% tin,
Bronze with 0.3-1% phosphorus, balance copper, e.g. UE9P
made of bronze. These materials can be used if the ethylene of the compressed fluid does not contain any traces of abrasive particles.
これに対して、被圧縮流体が上記3つの条件の
少なくとも1つに該当する場合には、普通に用い
られている材料で各部品を作つた往復圧縮機は満
足に運転できない。すなわち、故障なしに運転し
得る時間は数百であり、潤滑しない場合および/
または流体中に摩耗性粒子が含まれている場合に
は数十時間である。この欠点の原因を分析するた
めに、光学顕微鏡および電子顕微鏡で密封エレメ
ントの表面を調べた結果、圧縮機の密閉エレメン
トの摩耗の原因は密閉エレメントの表面が極めて
急速に損耗するためであることが分かつた。 On the other hand, if the fluid to be compressed meets at least one of the above three conditions, a reciprocating compressor whose parts are made of commonly used materials cannot operate satisfactorily. That is, the number of hours of operation without failure is in the hundreds, and without lubrication and/or
Or several tens of hours if the fluid contains abrasive particles. In order to analyze the cause of this shortcoming, we examined the surface of the sealing element using an optical and electron microscope and found that the cause of wear in the sealing element of a compressor is that the surface of the sealing element wears out very quickly. I understand.
発明が解決しようとする課題
本発明の目的は、上記3つの条件の少なくとも
1つに該当する流体を往復圧縮機で150バール以
上の圧力に圧縮する場合の技術上の諸問題点を解
決するこにある。Problems to be Solved by the Invention The purpose of the present invention is to solve various technical problems when compressing a fluid that meets at least one of the above three conditions to a pressure of 150 bar or more using a reciprocating compressor. It is in.
課題を解決するための手段
本発明は、少なくとも1つのピストンプランジ
ヤーまたはシリンダジヤケツトと、少なくとも1
つの密封エレメントとを有するエチレン重合法で
用いられる流体を極めて高い圧力に圧縮するため
の往復圧縮機において、少なくともピストンプラ
ンジヤーまたはシリンダジヤケツトと密封エレメ
ントとが互いに接触する部分が、80〜99重量%の
タングステン、クロムおよびチタンからなる群の
中から選択される金属の炭化物、窒化物、酸化物
および硼化物の中から選択される少なくとも1種
の化合物と、1〜20重量%のコバルト、ニツケ
ル、アルミニウムおよびこれらの合金からなる群
の中から選択される少なくとも1種の金属バイン
ダとによつて構成される少なくとも1種の材料で
作られていることを特徴としている。SUMMARY OF THE INVENTION The present invention provides at least one piston plunger or cylinder jacket and at least one piston plunger or cylinder jacket.
In a reciprocating compressor for compressing fluids to extremely high pressures used in the ethylene polymerization process, the reciprocating compressor has two sealing elements, in which at least the portion where the piston plunger or cylinder jacket and the sealing element are in contact with each other has a weight of 80 to 99 mm. % of at least one compound selected from carbides, nitrides, oxides and borides of metals selected from the group consisting of tungsten, chromium and titanium, and 1 to 20% by weight of cobalt, nickel. , aluminum, and at least one metal binder selected from the group consisting of aluminum and alloys thereof.
作 用
本発明は上記材料をエチレン重合法で用いられ
る往復圧縮機の互いに相対移動する部材の材料と
して用いることによつて長時間トラブルなしに連
続運転運転することができるという発見に基づい
ている。Function The present invention is based on the discovery that by using the above-mentioned material as a material for members that move relative to each other in a reciprocating compressor used in the ethylene polymerization method, continuous operation can be performed for a long time without trouble.
本発明で用いられる材料自体は公知のものであ
り、それ自体は本発明の対象をなすものではな
い。 The materials used in the present invention are known per se and are not subject to the present invention.
本発明では、密封エレメントを構成する材料と
ピストンプランジヤーまたはシリンダジヤケツト
を構成する材料とが同一の材料で作られている。
なお、密封エレメントを構成する材料とピストン
プランジヤーまたはシリンダジヤケツトを構成す
る材料との組成比を違えることもでき、場合によ
つては、これら2つの部品を構成する材料の2次
的特性、例えば金属バインダの結晶形、格子定数
および/または融点等を違えることもできる。 According to the invention, the material constituting the sealing element and the material constituting the piston plunger or cylinder jacket are made of the same material.
It should be noted that the composition ratio of the material constituting the sealing element and the material constituting the piston plunger or cylinder jacket can be different, and in some cases, the secondary properties of the materials constituting these two parts, For example, the crystal form, lattice constant, and/or melting point of the metal binder may be different.
金属バインダは面心立方晶系または最密充填六
方晶系の結晶形は有するものが好ましく、格子定
数は2.51〜4.10Åの範囲内で、融点は少なくとも
1453℃であるのが好ましい。 The metal binder preferably has a face-centered cubic crystal system or a close-packed hexagonal crystal system, a lattice constant within the range of 2.51 to 4.10 Å, and a melting point of at least
Preferably it is 1453°C.
本発明の往復圧縮機は下記のような条件下でも
2000時間以上の時間の間、全く問題無しに運転す
ることができる:
(a) 液体またはガスの被圧縮流体の温度が圧縮機
の全工程において−30〜+200℃の範囲にある
場合
(b) 流体の圧力が150バール以上である場合
(c) 圧縮機の部材の相対往復運動の平均速度が5
m/Sに達するような場合
(d) 摩擦係数が約0.5となる量の摩耗性粒子の痕
跡が被圧縮流体中に含まれている場合
(e) 被圧縮流体に自己潤滑性が無く、しかも外部
潤滑剤を補給できない場合。 The reciprocating compressor of the present invention can be used under the following conditions.
It can be operated without any problem for a period of more than 2000 hours: (a) if the temperature of the fluid to be compressed, liquid or gas, is in the range -30 to +200°C during the entire compressor process; (b) If the pressure of the fluid is greater than or equal to 150 bar, (c) the average velocity of the relative reciprocating motion of the compressor members is 5
m/S (d) When the compressed fluid contains traces of abrasive particles in an amount such that the coefficient of friction is approximately 0.5 (e) When the compressed fluid does not have self-lubricating properties and If external lubricant cannot be supplied.
本発明の対象とする流体は、圧縮機の全階段で
−30〜200℃の範囲の温度になる液体または気体
で、ヘリウム、アンモニウム等の種々の化学物質
でもよいが、本発明はエチレンとα−オレフイ
ン、水素または飽和炭化水素、例えばプロパン、
ブタンとの混合物に特に有利に適用することがで
きる。 The fluid targeted by the present invention is a liquid or gas that has a temperature in the range of -30 to 200°C in all stages of the compressor, and may be various chemical substances such as helium and ammonium. - olefins, hydrogen or saturated hydrocarbons, such as propane,
It can be applied particularly advantageously in mixtures with butane.
すなわち、本発明による往復圧縮機は化学工業
において種々の用途があるが、高圧下でのエチレ
ンの重合またはエチレンとα−オレフインとの共
重合に利用できる。 That is, the reciprocating compressor according to the present invention has various uses in the chemical industry, and can be used for polymerization of ethylene or copolymerization of ethylene and α-olefin under high pressure.
すなわち、エチレンの重合はチーグラー触媒系
の存在下で500バール以上の圧力で140〜300℃の
範囲の温度で行われることはフランス特許第
2021952号で公知である。高温高圧下でのエチレ
ン重合およびエチレンとα−オレフイン類との共
重合に用いられる触媒系は種々知られている。こ
れら触媒系は一般に少なくとも1種の遷移金属ハ
ロゲン化物と、元素周期律表の第〜族金属の
水素化物および有機金属化合物の中から選択され
る少なくとも1種の賦活剤とを含んでいる。使用
可能な遷移金属のハロゲン化物としてはクロム、
ジルコニウムおよびチタンのπ−アリルまたはベ
ンジル錯体、バナジウムおよびチタンのトリクロ
リド(これはTiCl3・1/3AlCl3の形の塩化アル
ミニウムの共晶になつている場合もある)があ
り、これらは必要に応じてマグネシウムのハロゲ
ン化物、モノハロゲン化物またはヒドロハロゲン
化物よりなる担体に担持させて用いられる。これ
らの化合物は、低級アルコール、金属アルコラー
ト、アルキルシリケート、アリールまたはアルキ
ルシロキサン、エーテルまたはアミン等の錯化剤
の存在下で使用することができる。使用可能な賦
活剤としてはトリアルキルアルミニウム、ハロゲ
ノジアルキルアルミニウムおよびアルキルシロキ
サンを挙げることができる。 Namely, it is stated in French patent no.
It is known from No. 2021952. Various catalyst systems are known for use in ethylene polymerization and copolymerization of ethylene and α-olefins under high temperature and high pressure conditions. These catalyst systems generally contain at least one transition metal halide and at least one activator selected from hydrides and organometallic compounds of metals of groups 1 to 1 of the Periodic Table of the Elements. Usable transition metal halides include chromium,
There are π-allyl or benzyl complexes of zirconium and titanium, trichlorides of vanadium and titanium (which may also be eutectic with aluminum chloride in the form TiCl 3 1/3 AlCl 3 ), which can be used as needed. It is used by being supported on a carrier made of a magnesium halide, monohalide, or hydrohalide. These compounds can be used in the presence of complexing agents such as lower alcohols, metal alcoholates, alkyl silicates, aryl or alkyl siloxanes, ethers or amines. Activators that can be used include trialkylaluminums, halogenodialkylaluminums and alkylsiloxanes.
上記の重合法または共重合法では、反応器から
の反応混合物が50〜500バールの圧力にある分離
器へ送られて、ポリマーと未反応モノマーとが分
離される。この分離器からのモノマーは反応圧ま
で圧縮されて反応器へ再循環される。 In the above polymerization or copolymerization methods, the reaction mixture from the reactor is sent to a separator at a pressure of 50 to 500 bar to separate the polymer and unreacted monomers. Monomer from this separator is compressed to reaction pressure and recycled to the reactor.
この場合、無視し得ない量の触媒残渣、特にア
ルミニウム化合物またはその他の還元性化合物を
含む低分子量のポリマーが、圧縮される未反応モ
ノマー流に随伴されるということが分かつてい
る。そのため、圧縮器の入口には粒径が1〜
250μmの低分子量のポリマー粒子が入り、この
低分子量のポリマー粒子が摩耗の原因となる。す
なわち、再循環される流体中の触媒残渣は圧縮さ
れて、その含有量は0.5ppm以上になる、圧縮機
の密封エレメントの摩耗の原因となる。 In this case, it has been found that non-negligible amounts of catalyst residues, in particular low molecular weight polymers containing aluminum compounds or other reducing compounds, are entrained in the compressed unreacted monomer stream. Therefore, at the inlet of the compressor, the particle size is
Low molecular weight polymer particles of 250 μm are included, and these low molecular weight polymer particles cause wear. That is, the catalyst residues in the recirculated fluid are compressed and their content reaches 0.5 ppm or more, causing wear of the sealing elements of the compressor.
従つて、本発明の往復圧縮機は、特に、反応器
中でチーグラー触媒系の存在下で200バール以上
の圧力且つ170℃以上の温度でエチレンを重合し、
反応器からの混合物を50〜500バールの圧力下に
ある分離器を送り、この分離器内でポリマーと未
反応エチレンとを分離し、分離器からのエチレン
を反応器の圧力まで加圧して反応器へ再循環する
エチレン重合法において、分離器からのエチレン
中に少なくとも0.5ppmの触媒系残渣を含んでい
るエチレンの重合法に使用することができる。本
発明の往復圧縮機を用いると、上記重合方法は高
い信頼度で運転することができる。 Therefore, the reciprocating compressor of the invention is particularly suitable for polymerizing ethylene in a reactor in the presence of a Ziegler catalyst system at a pressure of more than 200 bar and a temperature of more than 170°C;
The mixture from the reactor is sent to a separator under a pressure of 50 to 500 bar, in which the polymer and unreacted ethylene are separated, and the ethylene from the separator is pressurized to the pressure of the reactor and reacted. It can be used in ethylene polymerization processes where the ethylene from the separator contains at least 0.5 ppm of catalyst system residue in the ethylene polymerization process where the ethylene is recycled to the vessel. Using the reciprocating compressor of the present invention, the polymerization process described above can be operated with high reliability.
エチレンの重合は、例えば1〜50重量%のプロ
パンまたはブタン等の不活性炭化水素存在下およ
び/または2モル%以下の水素の存在下で実施す
ることができる。この重合は連続的に行われる
が、オートクレーブ、管状反応器等の任意の反応
器を使用することもできる。反応器は複数の反応
領域を有してもよい。本発明の往復圧縮機はエチ
レンとα−オレフイン、例えばプロピレンやブテ
ン−1等との共重合、あるいはエチレンと、α−
オレフイン、例えばプロピレンと、非共役ジオレ
フインとのターポリマーの重合でも使用すること
ができる。 The polymerization of ethylene can be carried out, for example, in the presence of 1 to 50% by weight of an inert hydrocarbon such as propane or butane and/or in the presence of up to 2 mol% hydrogen. This polymerization is carried out continuously, but any reactor such as an autoclave or a tubular reactor can be used. The reactor may have multiple reaction zones. The reciprocating compressor of the present invention is a copolymer of ethylene and α-olefin, such as propylene or butene-1, or ethylene and α-olefin.
It can also be used in the polymerization of terpolymers of olefins, such as propylene, and non-conjugated diolefins.
Claims (1)
はシリンダジヤケツトと、少なくとも1つの密封
エレメントとを有するエチレン重合法で用いられ
る流体を極めて高い圧力に圧縮するための往復圧
縮機において、 少なくともピストンプランジヤーまたはシリン
ダジヤケツトと密封エレメントとが互いに接触す
る部分が、80〜99重量%のタングステン、クロム
およびチタンからなる群の中から選択される金属
の炭化物、窒化物、酸化物および硼化物の中から
選択される少なくとも1種の化合物と、1〜20重
量%のコバルト、ニツケル、アルミニウムおよび
これらの合金からなる群の中から選択される少な
くとも一種の金属バインダとによつて構成される
少なくとも1種の材料で作られていることを特徴
とする往復圧縮機。 2 金属バインダが面心立方晶系または最密充填
六方晶系の結晶構造を有する特許請求の範囲第1
項に記載の往復圧縮機。 3 金属ハインダの格子定数が2.51〜4.10Åの範
囲内である特許請求の範囲第1または2項に記載
の往復圧縮機。 4 金属バインダの融点が1453℃以上である特許
請求の範囲第1〜3項のいずれか一項に記載の往
復圧縮機。 5 往復圧縮機の相対運動の平均速度が5m/s
以下である特許請求の範囲第1〜4項のいずれか
一項に記載の往復圧縮機。 6 流体を150バール以上の圧力に圧縮するのに
使用される特許請求の範囲第1〜5項のいずれか
一項に記載の往復圧縮機。 7 圧縮機の全階段での流体の温度が−30から+
200℃の間にある特許請求の範囲第6項記載の往
復圧縮機。 8 流体が痕跡の摩耗性粒子を含んでいる特許請
求の範囲第6または7項に記載の往復圧縮機。 9 流体に自己潤滑性無く且つ流体に外部潤滑剤
が添加されていない特許請求の範囲第6〜8項の
いずれか一項に記載の往復圧縮機。 10 流体に自己潤滑性が無く且つ流体に外部潤
滑剤は添加できるが外部潤滑剤の溶媒である特許
請求の範囲第6〜9項のいずれか一項に記載の往
復圧縮機。 11 流体がエチレンまたはエチレンとα−オレ
フイン、水素および飽和炭化水素からなる群の中
から選択される少なくとも1種の化合物との混合
物である特許請求の範囲第6〜10項のいずれか
一項に記載の往復圧縮機。 12 反応器中でチーグラー触媒系の存在下で
200バール以上の圧力且つ170℃以上の温度でエチ
レンを重合し、反応器からの混合物を50〜500バ
ールの圧力下にある分離器に送り、この分離器内
でポリマーと未反応エチレンとを分離し、分離器
からのエチレンを反応器の圧力まで加圧して反応
器へ再循環するエチレン重合法で用いられ、分離
器からのエチレン中に少なくとも0.5ppmの触媒
系残渣を含んでいるエチレンの重合法で使用され
る特許請求の範囲第11項記載の往復圧縮機。[Claims] 1. A reciprocating compressor for compressing fluids used in the ethylene polymerization process to very high pressures, which has at least one piston plunger or cylinder jacket and at least one sealing element, comprising at least one piston plunger or cylinder jacket and at least one sealing element. The part where the plunger or cylinder jacket and the sealing element are in contact with each other is made of 80-99% by weight of carbides, nitrides, oxides and borides of metals selected from the group consisting of tungsten, chromium and titanium. At least one compound selected from the above, and at least one metal binder selected from the group consisting of cobalt, nickel, aluminum, and alloys thereof in an amount of 1 to 20% by weight. A reciprocating compressor characterized in that it is made of seed material. 2. Claim 1 in which the metal binder has a face-centered cubic or close-packed hexagonal crystal structure
The reciprocating compressor described in Section. 3. The reciprocating compressor according to claim 1 or 2, wherein the metal binder has a lattice constant within the range of 2.51 to 4.10 Å. 4. The reciprocating compressor according to any one of claims 1 to 3, wherein the metal binder has a melting point of 1453°C or higher. 5 The average speed of relative motion of the reciprocating compressor is 5 m/s
A reciprocating compressor according to any one of claims 1 to 4 below. 6. A reciprocating compressor according to any one of claims 1 to 5, used for compressing a fluid to a pressure of 150 bar or more. 7 The temperature of the fluid at all stages of the compressor ranges from -30 to +
A reciprocating compressor according to claim 6, wherein the temperature is between 200°C. 8. A reciprocating compressor according to claim 6 or 7, wherein the fluid contains traces of abrasive particles. 9. The reciprocating compressor according to any one of claims 6 to 8, wherein the fluid does not have self-lubricating properties and no external lubricant is added to the fluid. 10. The reciprocating compressor according to any one of claims 6 to 9, wherein the fluid does not have self-lubricating properties and an external lubricant can be added to the fluid, but it is a solvent for the external lubricant. 11. According to any one of claims 6 to 10, wherein the fluid is ethylene or a mixture of ethylene and at least one compound selected from the group consisting of α-olefins, hydrogen, and saturated hydrocarbons. Reciprocating compressor as described. 12 In the presence of a Ziegler catalyst system in a reactor
Ethylene is polymerized at a pressure of more than 200 bar and a temperature of more than 170°C, and the mixture from the reactor is sent to a separator under a pressure of 50 to 500 bar, in which the polymer and unreacted ethylene are separated. is used in ethylene polymerization processes in which the ethylene from the separator is pressurized to the reactor pressure and recycled to the reactor, and where the ethylene from the separator contains at least 0.5 ppm of catalyst system residue. A reciprocating compressor according to claim 11, which is used legally.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR8307258 | 1983-05-02 | ||
FR8307258A FR2545544B1 (en) | 1983-05-02 | 1983-05-02 | ALTERNATE MOTION COMPRESSOR FOR VERY HIGH PRESSURES AND ITS APPLICATION TO A PROCESS FOR THE POLYMERIZATION OF ETHYLENE AND A-OLEFINS |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS59207908A JPS59207908A (en) | 1984-11-26 |
JPH0460131B2 true JPH0460131B2 (en) | 1992-09-25 |
Family
ID=9288468
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP7932484A Granted JPS59207908A (en) | 1983-05-02 | 1984-04-19 | Reciprocatory compressor available under high pressure and use for polymerization of ethylene-alpha-olefin polymerization |
Country Status (2)
Country | Link |
---|---|
JP (1) | JPS59207908A (en) |
FR (1) | FR2545544B1 (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2346669B (en) * | 1999-02-15 | 2002-12-18 | Ian Ross Walker | Pressure cell |
-
1983
- 1983-05-02 FR FR8307258A patent/FR2545544B1/en not_active Expired
-
1984
- 1984-04-19 JP JP7932484A patent/JPS59207908A/en active Granted
Also Published As
Publication number | Publication date |
---|---|
JPS59207908A (en) | 1984-11-26 |
FR2545544B1 (en) | 1987-04-03 |
FR2545544A1 (en) | 1984-11-09 |
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