CN1583716A - Preparing method for inactive nitric acid powder - Google Patents
Preparing method for inactive nitric acid powder Download PDFInfo
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- CN1583716A CN1583716A CN 200410026235 CN200410026235A CN1583716A CN 1583716 A CN1583716 A CN 1583716A CN 200410026235 CN200410026235 CN 200410026235 CN 200410026235 A CN200410026235 A CN 200410026235A CN 1583716 A CN1583716 A CN 1583716A
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- nitric acid
- urea
- urea nitrate
- inactive
- nitrate
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Abstract
A process for preparing non-active nitric acid powder includes such steps as adding nitric acid solution and urea to the mixture of acetic acid and sodium acetate solution, stirring, reacting to obtain urea nitrate, centrifugal separating of waste acid liquid, drying, adding corrosion inhibitor CM-911 and stirring. Dissolving it in water can become nitric acid.
Description
Technical Field
The invention relates to a chemical product for petroleum exploitation, in particular to a method for preparing inactive nitric acid powder.
Background
In oil field production, acidification is a common measure for removing oil layer blockage, the prior publicly known solution adopted in the acidification process mainly comprises traditional acid liquor such as hydrochloric acid, earth acid and the like, and can effectively remove oil channel blockage partially, but the main defects are that the blockage removing capability of the solution is poor, and the dissolution of rocks and clay is very limited. And when the amount or concentration of the acid liquid is not matched properly, new sediment blockage can be caused, secondary sediment is generated, and secondary pollution is caused.
Disclosure of Invention
The invention aims to overcome the defects of the traditional common acidification solution and provide a method for preparing inactive nitric acid powder for acidification and blockage removal.
The technical solution for realizing the aim of the invention is as follows: a method for preparing inactive nitric acid powder is characterized in that nitric acid solution and urea are added into a buffer solution system, the buffer solution system is formed by mixing acetic acid and sodium acetate solution, the mass ratio of the nitric acid solution to the urea solution is 1: 1, and the mixture is stirred at room temperature and reacts evenly to obtain intermediate urea nitrate; and then putting the reacted intermediate urea nitrateinto a centrifugal machine, throwing off the waste acid liquid, drying, adding the CM-911 type solid corrosion inhibitor, and uniformly stirring to obtain the finished product of the inactive nitric acid powder.
The process comprises the following steps:
1) taking a nitric acid solution with the concentration of 40-50% and urea, wherein the mass ratio of the nitric acid solution to the urea is 1: 1-3: 1;
2) adding the nitric acid solution into urea, then additionally adding a buffer solution system accounting for 0.3-1% of the total amount of the nitric acid solution and the urea, wherein the buffer solution system is formed by mixing acetic acid and a sodium acetate solution according to the mass ratio of 1: 1, uniformly stirring at room temperature, and standing for 12-36 hours to fully react;
3) after the reaction, putting the intermediate urea nitrate into a centrifugal machine, and throwing off the waste acid liquid to obtain the intermediate urea nitrate;
4) drying the intermediate urea nitrate, adding a CM-911 solid corrosion inhibitor accounting for 0.1-2.0% of the total amount of the urea nitrate, and uniformly stirring to obtain a finished product of inactive nitric acid powder; or the CM-911 solid corrosion inhibitor accounting for 0.1 to 2.0 percent of the total amount of the urea nitrate is additionally packaged into small packages and is subpackaged into finished product bags of intermediate urea nitrate to obtain finished product inactive nitric acid powder.
The preparation method is simple and practical, and the prepared solid white powder is inactive in solid state, has no corrosivity, is convenient to transport, and has low finished product price; when in use, the nitric acid is hydrolyzed into nitric acid when meeting water.
Detailed Description
The present invention is described in further detail below with reference to examples given herein.
According to the method, 50-100 parts by mass of urea and 0.5-2 parts by mass of a buffer solution system (formed by mixing acetic acid and a sodium acetate solution in a mass ratio of 1: 1) are added into 50-300 parts by mass of 40-50% (mass concentration) nitric acid solution, and the mixture is stirred and reacted for 12-36 hours at room temperature. And (4) throwing off the waste acid liquor to obtain the intermediate urea nitrate. And (3) drying the intermediate, adding 0.5-2 parts of CM-911 type solid corrosion inhibitor, and uniformly stirring to obtain a finished product of inactive nitric acid powder.
Or packaging CM-911 solid corrosion inhibitor into bags to obtain inactive nitric acid powder.
The production principle of the intermediate urea nitrate is as follows:
The finished product of the inactive nitric acid powder prepared by the method is solid white powder, is inactive in solid state, has no corrosivity and is convenient to transport; the finished product is hydrolyzed into nitric acid when meeting water, namely the reduction process is as follows: (ii) a And, as the product nitric acid is consumed, the hydrolysis reaction proceeds to the right. In specific acidizing applications, urea nitrate is carried in part solid form into the oil circuit channels of the oil reservoir, with the consumption of the hydrolysis nitric acid as it reacts with the rock components of the oil reservoir, the hydrolysisreactionContinuously proceeding to the right, and continuously reacting the newly generated nitric acid to achieve the effect of slow release, which is equivalent to a slow acid system; the inactive nitric acid powder has good compatibility with other acid solution, especially with hydrochloric acid solutionForm aqua regia and play a role in high corrosion rate.
Example 1: adding 100 kg of 50% (mass concentration) nitric acid solution into an acid-resistant tank, then adding 50 kg of urea and 0.5 kg of buffer solution system (acetic acid and sodium acetate solution are mixed according to the mass ratio of 1: 1), uniformly stirring, and standing overnight.
And (3) putting the materials into a centrifugal machine, and throwing off the waste acid liquor to obtain 75 kg of intermediate urea nitrate. And (3) putting the urea nitrate into a dryer, and drying by air blowing at 40 ℃ for 5-6 hours. Drying, adding into a stirrer, finally adding 0.60 kg of solid corrosion inhibitor CM-911, and uniformly stirring to obtain a finished product of inactive nitric acid powder.
Or directly packaging the dried urea nitrate into a finished product bag, and separately packaging the CM-911 type solid corrosion inhibitor into small packages, subpackaging into a finished product bag of the intermediate urea nitrate, and mixing with the intermediate urea nitrate when in use.
Example 2: 100 kg of 40 percent (mass concentration) nitric acid solution is added into an acid-resistant tank, then 60 kg of urea and 0.5 kg of buffer solution system (acetic acid and sodium acetate solution are mixed according to the mass ratio of 1: 1) are added, the mixture is uniformly stirred and is kept stand overnight.
And (3) putting the materials into a centrifugal machine, and throwing off the waste acid liquor to obtain 70 kg of an intermediate product urea nitrate. And (3) putting the urea nitrate into a dryer, and drying by air blowing at 40 ℃ for 5-6 hours. Drying, adding into a stirrer, finally adding 0.56 kg of CM-911 type solid corrosion inhibitor, and uniformly stirring to obtain a finished product of inactive nitric acid powder.
Or directly packaging the dried urea nitrate into a finished product bag, making another small package of the CM-911 type solid corrosion inhibitor, subpackaging into a finished product bag of the intermediate urea nitrate, and uniformly mixing with the intermediate urea nitrate when in use to obtain the inactive nitric acid powder finished product.
The above is a preferred embodiment of the present invention, and the present invention is not limited to the above embodiment, and the prepared inactive nitric acid powder can be obtained within the range of the compounding ratio of the technical solution of the present invention.
Claims (3)
1. A method for preparing inactive nitric acid powder is characterized in that nitric acid solution and urea are added into a buffer solution system, and are stirred uniformly at room temperature to react to obtain intermediate urea nitrate; and then putting the reacted intermediate urea nitrate into a centrifugal machine, throwing off the waste acid liquid, drying, adding the CM-911 type solid corrosion inhibitor, and uniformly stirring to obtain the finished product of the inactive nitric acid powder.
2. The method of claim 1, wherein the process comprises the steps of:
1) taking a nitric acid solution with the concentration of 40-50% and urea, wherein the mass ratio of the nitric acid solution to the urea is 1: 1-3: 1;
2) adding the nitric acid solutioninto urea, then additionally adding a buffer solution system accounting for 0.3-1% of the total amount of the nitric acid solution and the urea, uniformly stirring at room temperature, and standing for 12-36 h to fully react; after the reaction, putting the intermediate urea nitrate into a centrifugal machine, and throwing off the waste acid liquid to obtain the intermediate urea nitrate;
3) drying the intermediate urea nitrate, adding a CM-911 solid corrosion inhibitor accounting for 0.1-2.0% of the total amount of the urea nitrate, and uniformly stirring to obtain a finished product of inactive nitric acid powder; or the CM-911 solid corrosion inhibitor accounting for 0.1 to 2.0 percent of the total amount of the urea nitrate is additionally packaged into small packages, and the small packages are subpackaged into finished product bags of intermediate urea nitrate and are evenly mixed with the intermediate urea nitrate when in use to obtain the finished product of the inactive nitric acid powder.
3. The method for producing inactive nitric acid powder according to claim 1 or 2, wherein the buffer solution system is a mixture of acetic acid and sodium acetate solution, and the mass ratio is 1: 1.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200410026235 CN1244553C (en) | 2004-06-14 | 2004-06-14 | Preparing method for inactive nitric acid powder |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200410026235 CN1244553C (en) | 2004-06-14 | 2004-06-14 | Preparing method for inactive nitric acid powder |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1583716A true CN1583716A (en) | 2005-02-23 |
| CN1244553C CN1244553C (en) | 2006-03-08 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200410026235 Expired - Fee Related CN1244553C (en) | 2004-06-14 | 2004-06-14 | Preparing method for inactive nitric acid powder |
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| CN (1) | CN1244553C (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103145587A (en) * | 2012-12-27 | 2013-06-12 | 李无为 | Method for synthesizing powdered nitric acid by using allantoin synthetic waste liquid |
| CN103710171A (en) * | 2013-12-12 | 2014-04-09 | 内蒙古河西航天科技发展有限公司 | Acidic solid cleaning agent and preparation method thereof |
| CN106281273A (en) * | 2015-05-15 | 2017-01-04 | 中国石油天然气股份有限公司 | A kind of acid fluid system for being acidified carbonate reservoir |
-
2004
- 2004-06-14 CN CN 200410026235 patent/CN1244553C/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103145587A (en) * | 2012-12-27 | 2013-06-12 | 李无为 | Method for synthesizing powdered nitric acid by using allantoin synthetic waste liquid |
| CN103710171A (en) * | 2013-12-12 | 2014-04-09 | 内蒙古河西航天科技发展有限公司 | Acidic solid cleaning agent and preparation method thereof |
| CN106281273A (en) * | 2015-05-15 | 2017-01-04 | 中国石油天然气股份有限公司 | A kind of acid fluid system for being acidified carbonate reservoir |
| CN106281273B (en) * | 2015-05-15 | 2019-09-06 | 中国石油天然气股份有限公司 | It is a kind of for being acidified the acid fluid system of carbonate reservoir |
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| Publication number | Publication date |
|---|---|
| CN1244553C (en) | 2006-03-08 |
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Owner name: SHANXI HUAZE INDUSTRY CO.,LTD. Free format text: FORMER OWNER: FUAOTE INDUSTRIAL CO., LTD., SHAANXI PROV. Effective date: 20060324 |
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Effective date of registration: 20060324 Address after: 710075 hi tech Development Zone, Shaanxi Patentee after: Shaanxi Huaze Industrial Co., Ltd. Address before: 710075 hi tech Development Zone, Shaanxi Patentee before: Fuaote Industrial Co., Ltd., Shaanxi Prov. |
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Granted publication date: 20060308 Termination date: 20100614 |