专利摘要:
A process for preparing a polymer solution for use in "polymer based" oil recovery comprises adding to water the polymer in the form of an aqueous solution, a dry particulate solid or a suspension in a non-aqueous liquid, and also adding a complexing agent for multivalent ions and, where the solution so formed does not already contain an alkali metal salt, subsequently incorporating therein an alkali metal salt. The polymer may be a substantially cell-free microbial polysaccharide gum, a polyacrylamide or a cellulose derivative.
公开号:SU1215624A3
申请号:SU792784251
申请日:1979-06-22
公开日:1986-02-28
发明作者:Вильям Пейс Гари;Джон Холдинг Тревор
申请人:Геркулес Инкорпорейтэд (Фирма);
IPC主号:
专利说明:

"
The invention relates to chemical technology, namely to the process of obtaining polymer solutions for use in the extraction of oil and the use of complexing agents in such processes,
The purpose of the invention is the preparation of solutions for the recovery of oil with increased filterability.
Example 1 Xanthan fermentation broth (obtained by fermentation of Xanthotoonas compestria) is diluted and centrifuged to remove cell fragments. Prepare the following solutions:
q. diluting the stock solution with a solution of sodium chloride to the content of the latter and a solution of 3% and 0.1% polymer (control);
B. diluting the initial solution with a solution of the complexing agent sodium hexametaphosphate "by introducing solid sodium chloride to obtain a solution containing 0.25% sodium hexametaphosphate, 3% sodium chloride, 0.1% polymer and the rest is water,
The injection capacity of the solutions was evaluated by filtration under a pressure of 1.406 kg / cm at room temperature through a pre-filter Ap 200 Millipore and through a filter 0.8 µm Millipore and measurement of the filtration rate. The degree of filtration is determined at various volumes.
The results are presented in table. one
Example 2. Preparation of hydroxyethylcellulose (SCE) solutions:
01, 0.2% OEC in 3% solution - sodium chloride (control);
B. 0.2% OEC in solution with 0.2% sodium hexametaphosphate, followed by 3% sodium chloride.
The filterability of the solutions is assessed as in Example 1,
Results are presented in
tab. 2, 1
Measure 3, Prepare solutions of a -1,3-glucan resin prepared using the fungus Sclerotium glucanicum of the following composition:
cf, 0.2% polymer in 3% sodium chloride solution (control);
B. 0.2% polymer in a solution of 0.2% sodium hexametaphosphate followed by the introduction of sodium chloride,
242
The filterability of the solutions is determined as in Example 1
The results are presented in table, 3,
Example 4 The effect of sodium hexametaphosphate on op- was determined. tical purity of 1% polymer solutions,
The results are presented in table. four,
Example 5 The enzyme clarified xanthan gum is used to prepare aqueous solutions:
about. 0.2% polymer and 3% sodium chloride (control) j
B. 0.2% polymer, 2.92% ethylenediaminetetraacetic acid (EDTA) and 3% sodium chloride added last.
The filterability of the solutions is spread as in Example 1,
The results are presented in Table 5.
Example 6 The effect of the order of mixing the solution components is determined. To do this, prepare 0.1% solutions of xanthanum, precipitated by centrifugation, in the following manner:
a, the polymer is dissolved in a 3% solution of sodium chloride j
B, the polymer is dissolved in a 3% solution of sodium chloride and then O {2% sodium hexametaphosphate is added.
c, the polymer is dissolved in 0.2% sodium hexametaphosphate solution, and then 3% sodium chloride is added,
The filterability of the solutions is determined as in Example 1,
The results are presented in Table 6; From Table 6, it can be seen that the best result was achieved with the introduction of a complex-forming agent before chlo-
sodium hydroxide.
Example 7, Example 1 is repeated using polyacrylamide for the production of DM1 type oil, Hyper-floor, Preparing solutions:
a, 0.1% polymer and 3% sodium chloride 5
bt 0.1% polymer and 0.25% sodium hexametaphosphate followed by the addition of 3% sodium chloride. The filterability is determined as in
Example I using the pre-filter AR 2004200 Millipore, The results are shown in Table 7.
3
Example A 1% solution of xanthan, a new resin clarified using trifugation prices, is prepared in a concentrated (approximately 10%) solution of sodium hexamstaphosphate. As a control, the same t% solution in fresh water (not containing hexametaphosphate) is prepared. Both solutions are diluted with a strong solution (2% NaC 0.2% CaClp to obtain solutions: 0. 0.1% polymer solution in a brine; B. 0.1% polymer + 1% NaHMF in a strong brine.
The ability to filter ethic solutions assessed as in example 1.
The results are shown in Table. eight,
Example 9 The method of example 8 is repeated, but instead of strong brine, seawater is used (taken from the south coast of England and filtered through a millipolar filter with a hole diameter of 5 µm).
The results are shown in Table. 9.
Example 10. A concentrated solution of sodium hexametaphosphate is added to xanthan fermentation broth (approximately 2.5% xanthan gum) to obtain a 1: 1 ratio by weight of polymer to complexing agent, diluting the broth with an equal volume of fresh water. Both solutions were centrifuged to remove the cells, and then isopropanol was added to cause the xanthan gum and complex-forming reagent to precipitate together. The product is dried and crushed. Get the following solutions:
but. control: 0.01% polymer
in 3% NaCl;
J
Ltr rate, MP
Volume through the filter, ml
50 75 100 50
24
b. 0.1% polymer, 0.2% NaHMP, co-precipitated polymer in 3% NaCl.
Filtration capacity was measured as in Example 1.
The results are shown in Table. Ijl, - In examples 1-3, 5 - 7, the following can be used (see components with results similar to those indicated:
Polymer (0.1%)
Salt (3%)
five
Xanthan
0
Hydroxyethyl - 5 cellulose
- ..
NaCl
NajjSO
NaHCO,
NaCl
- -NaHCO
0 -1.3-GlucanNaCl
NaHCOj
n
Complex-former (0,2Z)
NEDTA-Na Citrate Na Gluconate
Thiourea
a Na tartrate
Trie Tanolamine
Ethilksa K
EDTA-Na Trip-Na Citrate On
(NEDTA-Ka-hydroxyethylene diamine triacetic acid, sodium salt, EDTA-Na ethylene diamine tetra acetic acid, sodium salt,
Trip-Na-sodium tripolyphosphate).
Table 1


Solution b
2.2 2.0 1.9 1.5
Table 2 st filtration, ml.
Solution. Solution (control)
1.0 1.4
0.8 1.3 0.7 1.1
g
Tables, tsa 3 orost filtration, ml-s
Solution a Solution b (control)
1.61.9
1,01,5
0.61.2
I
Table 4 Colorimeter readings
without hexamet-, 1% sodium hexamephosphate sodium taphosphate
0.75 0.45
0, 65 0.20
Bacterial cells are removed by enzyme treatment.
Filtration rate, mln.
Table 5
 . . T a b l and. C and 6
Table 7
Filtration rate, ml / s
Volume through the filter, ml
50 100 150 180
Filtration Table 9, mln.
Solution eaten Solution b. (control)
, 61
0.30.39
0,210.29
0.160.24
Table 10: Filtration ml.
Solution a Solution b (control)
 about 37 1.7
0.13 0.78
Editor M. Dylsh
Compiled by T. Martinska
Tehred Z. Patshy Corrector V. Butt ha,
Order 916/63 Circulation 47 Subscription
VNIIPI State Committee. the USSR
for inventions and discoveries 113035, Moscow, Zh-35, Raushsk office, 4/5
Filial ShSh Patent, g, Uzhgorod, st. Project, 4
1215624 O
Table 8
Solution (3 (control)
Solution b

0.94 0.64 0.48 0.39
权利要求:
Claims (1)
[1]
METHOD FOR PRODUCING A POLYMERIC SOLUTION FOR OIL RECOVERY, including mixing the polymer with additives and water, characterized in that, in order to obtain a solution with high filterability, hydroxyethyl cellulose, xanthan gum, p -1,3-glucan resin or polyacrylamide are used as a polymer , as additives - a complexing agent for divalent and trivalent metal cations - and an alkali metal salt selected from the group: chloride, sulfate or sodium bicarbonate, in the following ratio, wt.%:
Polymer 0.1-0.2
Complexing agent 0.2-2.92
Alkali metal salt selected from the specified group 2.0-3.0 r
Water The rest ® and mixing is carried out first by introducing the polymer or its aqueous solution into an aqueous solution of a complexing agent, and then the alkali metal salt. *>
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同族专利:
公开号 | 公开日
FR2429236A1|1980-01-18|
MX153483A|1986-11-07|
US4265673A|1981-05-05|
CA1113233A|1981-12-01|
NO150695B|1984-08-20|
FR2429236B1|1985-07-26|
NO792092L|1979-12-28|
NO150695C|1984-11-28|
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法律状态:
优先权:
申请号 | 申请日 | 专利标题
GB7827803|1978-06-23|
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