• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
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    • 专利摘要:
    A method for separating water-containing oil-based oil emulsions by mixing them with a demulsifier with co-alkylene oxide blocks, characterized in that, in order to increase the degree of separation, it is necessary to set up an excess of ethylene oxide blocks containing alkylenoxide blocks with an ethylene oxide block. HO- (CH2-CHO) - (CH2-CHO) p- (CH2-CH20) H CHd where p is 27.6-60, ff + n is such that the proportion of hydroxyethyl groups is 10-80% of the molecules - S block mass of the polymer, to the bisglycidyl ester of the general formula / f CHaT CH-CHfO O where 0-6, oxyalkylated with propylene oxide or butylene oxide or ethylene oxide and propylene oxide to a content of hydroxypropylene or hydroxybutylene groups of 17.7-75% and hydroxyethylene groups of 13.5-46.5% of molecular weight, in the amount of 20-50 million .
    公开号:SU1097201A3
    申请号:SU813368801
    申请日:1981-12-28
    公开日:1984-06-07
    发明作者:Дьери Хельмут；Хилле Мартин
    申请人:Хехст Аг (Фирма)；
    IPC主号:
    专利说明:

    This invention relates to methods for the separation of water-based oil emulsions. Most of the added oil is a water-in-oil emulsion. Only at the initial stage of oil field exploitation almost pure oil is produced. After some time, the water content in the oil increases, and this phenomenon begins to manifest itself predominantly in wells located on the edge of the oil field. Before transporting, the water must be removed from the oil, or its concentration must be reduced at least to the permissible concentration. In most cases, this is accomplished by adding a small amount of surfactants, called demulsifiers or emulsion breakers, with most of the oil being heated. Well as before, demulsifiers reduce to the required values the water content in the oil the oil content in the separated water and the salt and ash content in the oil at the lowest possible applied concentration and low temperature, and the same in a short time. The oil extracted in different parts of the earth is very different from one another, therefore, in order to achieve an optimal demulsification effect, emulsions of various types can be destroyed. In the case of large quantities of the oil emulsion extracted and to be processed, it is of great interest to use demulsifiers with improved properties, since a slight decrease in temperature during processing, salt and water content in oil, or oil content in water provides significant advantages in economic terms. A large group of demulsifiers are block polymers and copolymers derived from propylene oxide and ethylene oxide. There is a known method of destroying water-in-oil emulsions by adding to them a block polymer of ethylene oxide and propylene based on dihydric alcohols, for example diethylene glycol Сtj. It is very common to demulsify oil by reacting alkylene oxides with alkylphenol-formaldehyde resins. A known method for the separation of water-containing oil emulsions by the addition of ethoxylated nonylphenol-formaldehyde resin C2D as a demulsifier. The disadvantage of these methods is that the degree of destruction is not high enough. The purpose of the invention is to increase the degree of separation of water-containing oil emulsions. This goal is achieved by the method of separation of water-containing oil emulsions by mixing them with a demulsifier, the product of the addition of a block polymer of ethylene oxide and propylene oxide of the general formula HO- (CH2-CH20) (CH2 -CHIO) (CH2-CH20) H where p 27.6-60, i + n is such that the proportion of the hydroxyethyl groups is 10-80% of the molecular weight of the block polymer, to the bis-glycyyl ester of the general formula
    where a 0-6,
    oxyalkylated with propylene oxide or butylene oxide or ethylene oxide and propylene oxide to an oxypropylene or oxybutylene group of 17.7-75% of an ethylene-ethylene group of 13.6-46.5% of molecular weight, in an amount of 20-50.
    The bulk polymers obtained from ethylene oxide and propylene oxide are those that are obtained by ethoxylation of polyoxypropylene with a molecular weight of 1600-3500. The amount of ethylene oxide groups in the whole block polymer molecule is chosen in such a way that it is 10-80 wt.%. Bis-glycidyl ether is obtained in a known manner from the corresponding bisfgnol-2,2-bis- (4-hydroxyphenyl) propane. In addition, epoxy resins corresponding to formula (II) can also be used as bis-glycidyl ether. The block polymer obtained from ethylene oxide and propylene oxide interacts with bisglycidyl Bbw ether at a temperature between 70 and 160 ° C, preferably at 80-120 ° C. In most cases, the reaction is carried out in the absence of a solvent, however the reaction can also be carried out in an inert organic solvent. The molar ratio of the block polymer obtained from propylene oxide and ethylene oxide to the bisepoxy compound can be, for example, in the range of 1: 0.6 - 1: 1, and the ratio 1: 1 should not be exceeded. a crosslinking reaction occurs, resulting in a gelatinous product. Moreover, in some cases it is advisable to add the entire amount of the bis-epoxy compound in two or three portions during the reaction. The reaction is carried out in the presence of a catalyst having an alkaline reaction or Lewis acid. If the block polymer already contains an alkaline catalyst in the form of a neutral salt, used in the preparation of a block polymer, this salt acts as a catalyst when interacting with bisphenol. In this case, the additional addition of the catalyst is redundant. If the block polymer, after preparation, is free from the presence of a catalyst, then the catalyst of these types is necessary. The reaction time depends on the temperature at which the reaction is carried out. The reaction is carried out until the epoxy number is lower. 1-2. The addition products obtained by this method are directly subsequently oxyalkylated by alkylated oxide, for which one mainly uses propylene oxide, butylene oxide or propylene oxide, and ethylene oxide. In this case, as is well known for such mixed oxyalkylation, go three different ways. Thus, it is possible to first introduce the entire amount of propylene oxide into the addition reaction, then carry out oxyalkylation with ethylene oxide, or vice versa, first add all the desired amount of ethylene oxide and only then add the total amount of propylene oxide. In addition, there is the possibility that the adduct in a single step is oxyalkylated with a mixture containing the desired amounts of propylene oxide and ethylene oxide. The amount of propylene oxide or butylene oxide is measured in such a way that the amount of this alkylene oxide, attached at the last stage, is 17.7-75%, based on the molecular weight of the addition product, subjected to oxyalkylation. If ethylene oxide is additionally introduced into the addition reaction in the last step, the amount of ethylene oxide may be 13.5-46.5% (based on the weight of the addition product, including the amount of propylene oxide added at the end). Oxyalkylation in all cases is carried out under ordinary conditions when alkali is used as a catalyst. This reaction can be carried out at atmospheric pressure or alternatively under pressure in an autoclave. In the latter case, the operating pressure is 2-8 bar. The demulsifiers according to the invention in the case of different oil emulsions, upon demulsification, give better results than the results obtained by using known demulsifying agents. Especially important is the advantage of new demulsifiers in comparison with the known ones with a decrease in the residual salt content in the oil. The demulsifiers can be used as such or in the form of solutions that are diluted to a ratio of 1: 200 with an organic solvent. The concentration of the demulsifiers used in the separation of oil emulsions is in the range of 20-50 million.
    The examples below describe the preparation of adducts from bis-glycidyl ether of formula (H) and block polymers of ethylene oxide and propylene oxide of formula (1), used as starting materials in the synthesis of oxyalkylated products corresponding to the invention.
    Example 1. In a cylindrical vessel with thin sections, having a capacity of 1 liter and equipped with a root agitator, a thermometer inserted into the inside and a refrigerator with a tube filled with calcium chloride that prevents moisture from entering, place 561 parts by weight obtained from ethylene oxide and propylene oxide of the block polymer Formula (I), where p is 31.1 and 40% polyoxyethylene throughout the molecule (Genapol PF 40, average molecular weight 2805 is calculated from hydroxyl 1 in the number 40) and 45.1 weight parts. bis (glycidyl ether) of formula (11), wherein a is O (bisphenol A bis glycidyl ether, molecular weight 376 is calculated by the epoxy number). After stirring for 1/2 hour at room temperature, the reaction mixture is heated to a temperature inside the mixture (c) 80 ° C. After 8 hours, a second part of the bis-glycidipate ester is added, equal to 18.8 parts by weight. Then the mixture is stirred for another 8 hours at the same time and immediately afterwards for another 8 hours at 110 ° C. The total time during which the reaction is carried out is 24 hours. The epoxy number of the mixture at this is reduced to a value below 1-2. Point of cloudiness 64-65 C (in a mixture of butyldiglycol and water to DIN 53917). . Example 2. a) In a vessel with thin sections with a capacity of 2 liters, equipped with a root agitator, a refrigerator and a thermometer inserted inside, 623.2 parts by weight are placed. a block polymer of formula (I), where 40% of polyoxyethylen in the whole molecule (Pluriol PE 6400, molecular weight 3116 is calculated from the hydroxyl number) and 0.2008 parts by weight are mixed. etherata trifluoride boron, after which the reaction mixture is stirred for 15 min at room temperature. Directly
    but after this, 67.9 parts by weight are added to the mixture. bisphenol A bis (glycidyl ether) (molecular weight 376) and stirring the mixture for 10 hours at 120 ° C. The result is a yellow colored clear liquid having an average viscosity, and its epoxy number is about 1. Cloud point according to DIN 53917-41C.
    b) If the reaction is carried out using 8.2 parts by weight of boron trifluoride instead of etherate. sodium stearate with stirring for 15 hours at 140 ° C, then a turbid reddish-brown colored reaction product is obtained, which, when added 10 parts by weight. Celite (diatomaceous earth) can be filtered in a hot state to form a pure liquid. The cloud point according to DIN 53918 61 C, the epoxy number is less than 1. P, p and measure 3. If in example 2 (a) the bisphenol A bis-glycidyl ether is replaced by 336, 8 parts by weight an epoxy resin of formula (II), where, with an epoxy number of 39 and the reaction mixture is stirred for 28 hours at 120 ° C, the epoxy number of the reaction product will be reduced to 4-5. With a one-time addition of 0.2 weight.h. boron trifluoride etherate and further reacting with the epoxy number for less than 8 hours becomes less than 1. As a result, a yellow-colored liquid with high viscosity is obtained. Cloud point according to DIN 53917 -. Example 4. When replacing the epoxy resin used in example 3, 168,4 weight.h. an epoxy resin of the formula (I) where (af 2.4) with an epoxy number of 77/78, the stirring being carried out for 28 hours at, adding 0.2 parts by weight. boron trifluoride etherate; a clear, yellowish-colored liquid having a high viscosity is obtained. Cloud point according to DIN 53917. Example 5. a) In a vessel with thin sections with a capacity of 2 liters (described in Example 2c (), it is stirred for 8 hours at 975.6 parts by weight of the block polymer of formula (1) obtained from ethylene oxide and propylene oxide, where, 6 and 20% polyoxyethylene throughout the molecule (Genapol PF ZOl) and 89.3 parts by weight of bis-diglycidyl ether | of bisphenol A (epoxy number 196). Then 37.2 parts by weight of bis-glycidyl ether are added to the mixture. Bisphenol A and the reaction mass is stirred once more for 8 hours at and 8 hours at a temperature The liquid reaction product has an epoxide number less than 1, the point of cloudiness according to DIN 539t7 5lC. B) The block polymer used in Example 5e is replaced with 2301.6 parts by weight of the block polymer of formula (1) obtained from ethylene oxide and propylene oxide, where, 6 with 80% polyoxyethylene in the whole molecule Genapol PF 80 hydroxyl number 19/20). At the same time, the reaction time at 110 ° C is prolonged to 18 h. As a result, a wax-like product of white color with an epoxy number of approximately 1 is obtained. The cloud point according to DIN 53917 is 90 ° C. Example 6. A vessel with thin sections with a capacity of 2 liters (described in example 2) is placed 561 wee.h of the block polymer obtained in example 1 and 224.6 parts by weight of ethylene oxide and propylene oxide obtained. an epoxy resin (example 3) with an epoxy number of 39, after which the mixture is slowly stirred for 24 hours at 80 ° C. This reduces the epoxy number to 1. As a result, a product having a high viscosity is obtained. Example 7. In a vessel with grinding sections with a capacity of 1 l, it is stirred for 8 hours at a temperature of 437.5 parts by weight. ethylene and propylene oxide derived from a block polymer of formula (1), where 60% of polyoxyethylene is in the whole molecule with 67.0 parts by weight. bisphenol A bis-diglycidyl ether (molecular weight 372 is calculated by the epoxy number). Immediately thereafter, 27.9 parts by weight are added to the mixture. bis-diglycidyl ether. The reaction is carried out until the end by stirring the mixture for 8 hours at and for 8 hours at 110 ° C. The waxy reaction product painted in a light brown color has an epoxy number of 3. Cloud point according to DIN 53917 is 85 ° C. Example 8. 411,6 weight.h. a block polymer of formula (I), where p- 32 and 10% polyoxyethylene in the whole molecule (Pluriol HE 6100) are mixed in the apparatus described in Example 2 with 5.4 weight parts. isostearate sodium. Then, 67.0 parts by weight is added to the mixture. bisphenol A bis-glycidyl ether, after which the reaction mixture is stirred for 32 hours at. The epoxy number of the liquid reaction product is reduced to 1. In the following npiiMepax, the preparation of compounds used as demulsifiers is described by oxyalkylation of the addition products obtained in Examples 1-8. Example 9. a) In an autoclave with a capacity of 30 liters, equipped with a stirrer and an ETH temperature measuring device, 4454 parts by weight are placed. adherence product of Example 1, and 22.3 parts by weight. A 30% aqueous solution of sodium methylate in methyl alcohol, after which the apparatus is washed with nitrogen. During 4 hours at a mixture temperature of 160-180 ° C and at a pressure of 4.5 bar, 4774 parts by weight were introduced into the autoclave. propylene oxide, after which the stirring of the reaction mixture is continued at 150160 ° C for an hour. The product obtained as a result of the oxyhilder reaction contains 51.7% polyoxypropylene. By adding 15 pbw of glacial acetic acid, the pH of the product was adjusted to 7. The cloud point according to DIN 53917. b) If, under the conditions described in Example 9c, 2880 parts by weight an accessory product corresponding to example 1, oxypropylate using 620 parts by weight. propylene oxide, a red-brown colored liquid reaction product is obtained which contains 17.7% poly.oxypropylene. Cloud point according to DIN 53917 63-64 ° C. c) For example, 9c 2880 weight.h. the reaction product corresponding to example 1 is oxyalkylated with a mixture of 635 parts by weight. ethylene oxide and 1785 weight.h. propylene oxide, in the presence of 24 weight.h. 30% sodium methoxide solution. The reaction product contains 13.6% ethylene oxide and 37.0% propylene oxide as a mixed oxyalkylate and is a reddish-brown liquid. Cloud point according to DIN 53917. Example 10. a) In an aktoklav with a capacity of 2 l, equipped with a stirrer and a thermometer inserted inside, 435 parts by weight are placed. the reaction product obtained in Example 5o (from 2 parts by weight of a 30% aqueous solution of sodium metipate in methyl alcohol. At a temperature inside the reactor of 160-170 ° C and a pressure of 4-5 bar for 30 minutes, the autoclave is evacuated under a pressure of 180% the mixture is stirred for 1 hour, the brown colored reaction product, having an average viscosity, contains 29.2% polyoxypropylene. The kidney of turbidity according to DIN 53917 is approximately 38 ° C. b) conditions described in the example of Yua, 354 weight parts. applied in the same example, the source material input interaction with 213 weight.h. propylene oxide, as a result of which I get the reaction product of hydroxypropylation with 46.8% polyoxypropylene. The cloud point according to DIN 53917 is approximately 28 ° C. . Example 11. a) In the apparatus for oxyalkylation described in Example 10, 300 parts by weight. the reaction product obtained in accordance with Example 5 is reacted with 314 parts by weight of Oinei propylene. The result is a brown, soft colored product that contains 51.1% poly oxypropylene. The cloud point of DIN 53917 is approximately equal. b). If, by analogy with that described in Example 11, to apply such amount of propylene oxide so that as a result of the reaction, a product with 75.0% polyoxypropylene is formed, a paste-colored paste colored with a cloud point according to DIN 53917 approximately 10 ° C is obtained. Example 12. a) In the apparatus for oxyalkylation described in Example 10, 547 parts by weight are placed. the product of propylation obtained
    according to example 9c (,
    foot
    2 sodium methylate. With those of the reaction mixture at 160-180 ° C, 96.5 parts by weight were introduced into the apparatus. oxide of ethylene so that the final product additionally contains 15.0% polyoxyethylene throughout the molecule. The reaction product is co-alcohol reacted under normal conditions with 161 parts by weight. propylene oxide. The liquid reaction product contains 30.6% polyoxypropylene. Cloud point according to DIN 53917.
    Example 16. 350 weight.h. the interaction product obtained in accordance with Example 2a in the presence of a moderately viscous fluid. Cloud point according to DIN 53917. b) If, by analogy with that described in example 12o, such an amount of ethylene oxide is used so that a final product containing 29.3% polyoxyethylene is formed, then a liquid product with a cloud point according to DIN 53917 is obtained. c) If oxyethylation is carried out by analogy with that described in example 12a, but with such amount of ethylene oxide that 46.5% polyoxyethylene is additionally contained in the final product, then a product having a pasty consistency is obtained. Cloud point according to DIN 53917. Example 13. In an autoclave for oxyalkylation with a capacity of 2 liters, described in Example 10, 319 parts by weight the reaction product corresponding to example 3, in the presence of 10 weight.h. A 30% aqueous solution of sodium methylate in methyl alcohol is reacted with 123 parts by weight. propylene oxide, and the reaction is carried out first for 1 hour, then for 45 minutes at a temperature in the autoclave of 160-170 ° C at a pressure of 4-5 bar. After further stirring for 1 hour, a liquid viscous reaction product is obtained which contains 27.8% polyoxypropylene. Cloud point according to DIN 53917 32 ° C. Example 14. Under the conditions described in example 13, 246 parts by weight. the reaction product obtained in example 4, in the presence of 8 parts by weight A 30% aqueous solution of sodium methylate in methyl alcohol is reacted with 106 parts by weight. oxides of oxen. The liquid reaction product contains 29.2% polyoxypropylene. Cloud point according to DIN 53917. Example 15. In a 2-liter apparatus described in Example 10, 365 parts by weight. the reaction product obtained in accordance with example 6, in the presence of 5 parts by weight 30% aqueous solution of sodium methylate in the methyl part by weight.h. caustic soda is introduced into the reaction with 110 parts by weight. propipene oxides under pressure. The liquid reaction product contains 23.9% polyoxypropylene and has a cloud point according to DIN 53917. Example 17. In the apparatus for oxyalkylation described in Example 10, 476 parts by weight were placed. an addition product prepared according to Example 1 and 4.8 parts by weight. 30% sodium methylate solution in methyl alcohol. The oxyalkylation reaction is carried out in the usual manner using a mixture of 357 parts by weight. propylene oxide and 131 weight.h. ethylene oxide at a temperature inside the apparatus of 160-167 ° C and a pressure of 4-5 bar for 1 h. The pure red-brown colored liquid final product contains 36.8% of propylene oxide and 13.5% of ethylene oxide as a mixed oxyalkyl ta. Cloud point according to DIN 53917 Example 18. 424 parts by weight the addition product obtained in accordance with Example 1 in the presence of 7.0 parts by weight. sodium methoxide solution (30% solution in methypol alcohol), and methyl alcohol is distilled in a vacuum, introduced into the interaction in the apparatus for oxyalkylation described in Example 10, with 136 parts by weight. isobutylene oxide (2,2 dn-methyloxyran) under normal conditions. The reaction product contains 24.2% polyoxybutylene. After neutralization with glacial acetic acid to a pH of 6.1, a more pasty substance is obtained which is soluble in water to form a milky variety. Example 19. If Sb4 weight.h. the reaction product obtained according to the Example Example Amount of water,% released
    Table 1 with example 1, add to the interaction under the same conditions with 375 parts by weight. n-butylene oxide (n-butylene oxide-1,2) and immediately after that by adding glacial acetic acid the product pH is adjusted to 6.5, then a clear liquid reaction product is obtained, which dissolves in water to form a cloudy solution. The reaction product contains 50.6% polyoxybutylene. Example 20. 389 weight.h. the addition product obtained in accordance with Example 7 in the presence of 5 parts by weight. Sodium methylate solution (30% solution in methyl alcohol) is reacted under the conditions described in the examples above, with 382 parts by weight. propylene oxide. The product obtained as a result of the reaction contains 49.2% polyoxypropylene and is a brownish paste. Cloud point according to DIN 53917 24c. Example 21. Under normal conditions, 221 parts by weight the addition product obtained in accordance with Example 8 is introduced into the reaction of hydroxypropylation with 198 weight parts. propylene oxide. The product neutralized with glacial acetic acid is red-brown in color and does not dissolve in water. In tab. Tables 1-3 show the results obtained when three different oil emulsions were destroyed when using the products of Example 9-21 for the demulsifier used according to the invention as emulsifiers.
    13
    1097201
    14 Continued table. one
    Note. ., The temperature during the demulsification of the water content in the emulsion is 56%; dosage amount of demulsifier 40 ppm; place of production - Germany / Emsl nd. Note.
    Table 2 The temperature during the demulsification of the water content in the emulsion 42%; The dosed amount of demulsifier 20 dobpsh place - Saudi Arabi is easy. Note.
    Table 3 Temperature during demulsification 45 ° С; water content in the emulsion 42%; dosed quantity of demulsifier 50 production site - Iran.
    19109720120
    In each case, 50% water content in the emulsion was used, the temperature
    solutions of demulsifiers in methylenes when demulsifying and place of extraction
    alcohol, since pure substances of an emulsion emulsion are indicated in the note, which are high, after each table, viscosity and poorly dosed materials.
    ly. Due to the very small use of B-In addition, in the tables for cpdsmrs of amounts, the addition of 50% of the results are given. The results of the destruction of the solutions were made using pre-emulsions with oxyethylboron demulsifier for accurate dosing. The absolute nonylphenol-formaldehyde content of water in emulsions of the definite | 0 resin containing 5 units. ethylene oxide was preformed according to Dien-Rusku. on one phenolic ring according to the known dosage amount of the demulsifier method (example 22).
    权利要求:
    Claims (1)
    [1]
    METHOD FOR SEPARATING HYDRAULIC SODES ( LIVING OIL EMULSIONS by mixing them with a demulsifier containing
    СНа-СН-СНгО about
    where a = 0-6, oxyalkylated with propylene oxide or butylene oxide or ethylene oxide and propylene oxide to contain alkylene oxide blocks, characterized in that, in order to increase the degree of separation, the product of blocking the oxide polymer is used as a demulsifier containing alkylene oxide blocks ethylene and propylene oxide of the general formula but- (sn 2 -sn 2 o) t - (sn 2 -sn 2 ) - (sn 2 -sn 2 o H ' CH 9 where p = 27.6-60, w + n - such that the proportion of hydroxyethyl groups is 10-80% of the molecular weight of the block polymer, to bisglycyl ether ether of the general formula oxypropylene or oxybutylene groups of 17.7-75% and oxyethylene groups of 13.5-46.5% of the molecular weight, in the amount of 20-50 million “ 1 .
    SU,., 1097201
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    同族专利:
    公开号 | 公开日
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    引用文献:
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    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    DE19803049450|DE3049450A1|1980-12-30|1980-12-30|"OXALKYLATED ADDITION PRODUCTS FROM ETHYLENE-OXIDE-PROPYLENE-OXIDE BLOCK POLYMERS AND BIS-GLYCIDYL ETHERS AND THE USE THEREOF"|
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