CN107312567A - A kind of method of purification of chlorinated paraffin raw material wax oil - Google Patents
A kind of method of purification of chlorinated paraffin raw material wax oil Download PDFInfo
- Publication number
- CN107312567A CN107312567A CN201710654916.2A CN201710654916A CN107312567A CN 107312567 A CN107312567 A CN 107312567A CN 201710654916 A CN201710654916 A CN 201710654916A CN 107312567 A CN107312567 A CN 107312567A
- Authority
- CN
- China
- Prior art keywords
- wax oil
- raw material
- chlorinated paraffin
- purification
- magnetic filter
- 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.)
- Pending
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING 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
- C10G53/00—Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more refining processes
- C10G53/02—Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more refining processes plural serial stages only
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING 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
- C10G73/00—Recovery or refining of mineral waxes, e.g. montan wax
- C10G73/38—Chemical modification of petroleum
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Fats And Perfumes (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Treating Waste Gases (AREA)
Abstract
The present invention is a kind of method of purification of chlorinated paraffin raw material wax oil, and the method for purification comprises the following steps:(1)Raw material wax oil passes through magnetic filter for tube under certain flow velocity(1);(2)By step(1)Middle process magnetic filter(1)Wax oil be passed through the washer containing chlorine, chlorine hydride mixed gas body(2)Middle removal aromatic hydrocarbons and basic nitrogen;(3)By step(2)In product be passed through quantizer(3)Middle stratification goes the removal of impurity, obtains pure wax oil.The present invention realizes the method that the raw material wax oil of chlorinated paraffin removes impurity, and control is stable, impurity removal effect is good, and chlorinated paraffin product quality is significantly improved.
Description
Technical field
The present invention relates to a kind of method of purification, a kind of method of purification of chlorinated paraffin raw material wax oil is particularly related to.
Background technology
If chlorinated paraffin preparing raw material wax oil containing impurity can very more serious influence early to the preparation of chlorinated paraffin, at present
The most impurity-eliminating effect of impurity-removing method it is poor, it is stable under it is poor, had a strong impact on the quality that the later stage prepares chlorinated paraffin.
The content of the invention
In order to solve the above problems, the invention provides a kind of method of purification of chlorinated paraffin raw material wax oil, this method is removed
Miscellaneous effect is good.
In order to achieve the above object, the present invention is achieved by the following technical solutions:
The present invention is a kind of method of purification of chlorinated paraffin raw material wax oil, and the method for purification comprises the following steps:
(1)Raw material wax oil passes through magnetic filter for tube under certain flow velocity(1);
(2)By step(1)Middle process magnetic filter(1)Wax oil be passed through the washer containing chlorine, chlorine hydride mixed gas body
(2)Middle removal aromatic hydrocarbons and basic nitrogen;
(3)By step(2)In product be passed through quantizer(3)Middle stratification goes the removal of impurity, obtains pure wax oil.
Further improvement of the present invention is:The step(1)The flow velocity of middle wax oil is 1300-1500L/h.
Further improvement of the present invention is:In the step(2)Described in chlorine, hydrogen chloride gas be passed through gas flow
For 1500m3The ratio of chlorine and hydrogen chloride is volume ratio 0.5 in/h, gaseous mixture:100-3:100, the weight with wax oil intake
Than 1.2:1-1.3:1, time of washing be how long the 3-5min times, control temperature is at 60-90 DEG C.
Further improvement of the present invention is:In the step(3)In, the time of stratification is 3-4h.
A kind of purifying plant of chlorinated paraffin raw material wax oil, the device includes magnetic filter, the side of magnetic filter
Washer is connected with, the upper end of washer is provided with gas vent, quantizer is connected by pipeline in the lower end of washer, point
Exquisite wax oil outlet and hydrochloric acid gateway are additionally provided with layer device.
The beneficial effects of the invention are as follows:Raw material wax oil passes through magnetic filter for tube under certain flow velocity, due to magnetic
Suction-operated, remove tiny iron filings class impurity;Afterwards by containing chlorine, the washing of chlorine hydride mixed gas body, removing oxidizable
Aromatic hydrocarbons and basic nitrogen, stratification remove impurity, obtain pure wax oil.
The present invention realizes the method that the raw material wax oil of chlorinated paraffin removes impurity, and control is stable, impurity removal effect is good,
Chlorinated paraffin product quality is significantly improved.
Brief description of the drawings
Fig. 1 is the structural representation of purifying plant of the present invention.
Embodiment
In order to deepen the understanding of the present invention, the present invention is done below in conjunction with drawings and examples and further retouched in detail
State, the embodiment is only used for explaining the present invention, protection scope of the present invention is not constituted and limited.
As shown in figure 1, the present invention is a kind of method of purification of chlorinated paraffin raw material wax oil, the method for purification includes as follows
Step:
(1)Raw material wax oil passes through magnetic filter for tube under certain flow velocity(1), wherein, the flow velocity of wax oil is 1300-
1500L/h。
(2)By step(1)Middle process magnetic filter(1)Wax oil be passed through and washed containing chlorine, chlorine hydride mixed gas body
Wash device(2)Middle removal aromatic hydrocarbons and basic nitrogen;Wherein, the chlorine, the gas flow that is passed through of hydrogen chloride gas are 1500m3/ h, is mixed
The ratio for closing chlorine and hydrogen chloride in gas is volume ratio 0.5:100-3:100, compare 1.2 with the weight of wax oil intake:1-1.3:
1, time of washing be how long the 3-5min times, control temperature is 60-90 DEG C ' '
(3)By step(2)In product be passed through quantizer(3)Middle stratification goes the removal of impurity, obtains pure wax oil, wherein,
The time of stratification is 3-4h.
A kind of purifying plant of chlorinated paraffin raw material wax oil, described device includes magnetic filter 1, magnetic filter 1
There is the import of waxy stone oil side, and waxy stone oil is filtered by magnetic filter 1, and the side of the magnetic filter 1 is connected with washing
Device 2, gas vent is provided with the upper end of the washer 2, and there are chlorine, the entrance of chlorine hydride mixed gas body, gaseous mixture in lower end
Body is gone out from the upper end of washer again after entering from the lower end of washer 2, the effect washed to wax oil is realized, in the washer
2 lower end is connected by pipeline is additionally provided with exquisite wax oil outlet and hydrochloric acid gateway on quantizer 3, the quantizer 3.
Raw material wax oil passes through magnetic filter for tube under certain flow velocity, due to the suction-operated of magnetic, removes tiny
Iron filings class impurity;Afterwards by containing chlorine, the washing of chlorine hydride mixed gas body, removing oxidizable aromatic hydrocarbons and basic nitrogen, standing
Layering removes impurity, obtains pure wax oil.
Claims (5)
1. a kind of method of purification of chlorinated paraffin raw material wax oil, it is characterised in that:The method of purification comprises the following steps:
(1)Raw material wax oil passes through magnetic filter for tube under certain flow velocity(1);
(2)By step(1)Middle process magnetic filter(1)Wax oil be passed through the washer containing chlorine, chlorine hydride mixed gas body
(2)Middle removal aromatic hydrocarbons and basic nitrogen;
(3)By step(2)In product be passed through quantizer(3)Middle stratification goes the removal of impurity, obtains pure wax oil.
2. a kind of method of purification of chlorinated paraffin raw material wax oil according to claim 1, it is characterised in that:The step(1)
The flow velocity of middle wax oil is 1300-1500L/h.
3. a kind of method of purification of chlorinated paraffin raw material wax oil according to claim 1, it is characterised in that:In the step
(2)In, the chlorine, the gas flow that is passed through of hydrogen chloride gas are 1500m3The ratio of chlorine and hydrogen chloride is in/h, gaseous mixture
Volume ratio 0.5:100-3:100, compare 1.2 with the weight of wax oil intake:1-1.3:1, time of washing be how long 3-5min when
Between, control temperature is at 60-90 DEG C.
4. a kind of method of purification of chlorinated paraffin raw material wax oil according to claim 1, it is characterised in that:In the step
(3)In, the time of stratification is 3-4h.
5. a kind of purifying plant of chlorinated paraffin raw material wax oil according to claim 1, it is characterised in that:Described device includes
Magnetic filter(1), the magnetic filter(1)Side be connected with washer(2), in the washer(2)Upper end set
Gas vent is equipped with, in the washer(2)Lower end quantizer is connected by pipeline(3), the quantizer(3)On also set up
There are exquisite wax oil outlet and hydrochloric acid gateway.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201710654916.2A CN107312567A (en) | 2017-08-03 | 2017-08-03 | A kind of method of purification of chlorinated paraffin raw material wax oil |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201710654916.2A CN107312567A (en) | 2017-08-03 | 2017-08-03 | A kind of method of purification of chlorinated paraffin raw material wax oil |
Publications (1)
Publication Number | Publication Date |
---|---|
CN107312567A true CN107312567A (en) | 2017-11-03 |
Family
ID=60170123
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201710654916.2A Pending CN107312567A (en) | 2017-08-03 | 2017-08-03 | A kind of method of purification of chlorinated paraffin raw material wax oil |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN107312567A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108795496A (en) * | 2018-08-14 | 2018-11-13 | 常州星源新能源材料有限公司 | A kind of paraffin oil separating extraction device |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102145251A (en) * | 2011-01-06 | 2011-08-10 | 鲁西化工集团股份有限公司氯碱化工分公司 | Dechloridation device and process in chlorinated paraffin production process |
CN201949806U (en) * | 2011-01-06 | 2011-08-31 | 鲁西化工集团股份有限公司氯碱化工分公司 | Dechlorination device in process of producing chlorinated paraffin |
CN203956003U (en) * | 2014-06-24 | 2014-11-26 | 南京优耐特精密铸造有限公司 | A kind of wax cylinder with slack wax purification function |
CN106479567A (en) * | 2015-11-25 | 2017-03-08 | 衡阳市骏杰化工有限公司 | The technique that a kind of catalysis method produces chlorinated paraffin |
CN106800950A (en) * | 2015-11-25 | 2017-06-06 | 衡阳市骏杰化工有限公司 | A kind of refined production technology of atoleine |
-
2017
- 2017-08-03 CN CN201710654916.2A patent/CN107312567A/en active Pending
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102145251A (en) * | 2011-01-06 | 2011-08-10 | 鲁西化工集团股份有限公司氯碱化工分公司 | Dechloridation device and process in chlorinated paraffin production process |
CN201949806U (en) * | 2011-01-06 | 2011-08-31 | 鲁西化工集团股份有限公司氯碱化工分公司 | Dechlorination device in process of producing chlorinated paraffin |
CN203956003U (en) * | 2014-06-24 | 2014-11-26 | 南京优耐特精密铸造有限公司 | A kind of wax cylinder with slack wax purification function |
CN106479567A (en) * | 2015-11-25 | 2017-03-08 | 衡阳市骏杰化工有限公司 | The technique that a kind of catalysis method produces chlorinated paraffin |
CN106800950A (en) * | 2015-11-25 | 2017-06-06 | 衡阳市骏杰化工有限公司 | A kind of refined production technology of atoleine |
Non-Patent Citations (1)
Title |
---|
胡晓剑: ""液体石蜡精制及氯化石蜡-52生产工艺的改进"", 《工程科技I辑》 * |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108795496A (en) * | 2018-08-14 | 2018-11-13 | 常州星源新能源材料有限公司 | A kind of paraffin oil separating extraction device |
CN108795496B (en) * | 2018-08-14 | 2024-04-09 | 常州星源新能源材料有限公司 | Paraffin oil separation and extraction device |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN108607511A (en) | A kind of industrial waste-gas purifier using new waste gas adsorbent | |
CN105110668A (en) | Sea sand desalination treatment technique and system | |
CN207537264U (en) | A kind of movable type effluent treatment and filtering device | |
JP6659668B2 (en) | Method for producing deuterium-reduced water, method for separating heavy water and light water, and method for producing deuterium concentrated water | |
CN107312567A (en) | A kind of method of purification of chlorinated paraffin raw material wax oil | |
CN207356646U (en) | A kind of skid-mounted type integrated oil field filtering oily sewage tank filtering material cleaning device | |
CN106621495A (en) | Quartz sand filter | |
CN102826683A (en) | Sewage recycling processor | |
CN204981232U (en) | System for resin adsorbs handles waste water | |
CN106493391B (en) | A kind of method of purification of copper nano-wire | |
CN102327767B (en) | Filter medium for removing boron in water and preparation method thereof | |
CN207324425U (en) | Purifier for supercritical carbon dioxide Brayton cycle power generation system | |
CN109231337B (en) | Portable adsorption treatment device and treatment method for farmland low-concentration heavy metal-containing sewage | |
CN109772280B (en) | Method for removing trace glyphosate in drinking water source water | |
CN100534921C (en) | Method for treating wastewater containing metal ion by modified resin and desorption device thereof | |
CN205055517U (en) | Multi -media filter | |
CN206244538U (en) | A kind of tungsten water solid device for filtering impurities | |
CN109231592A (en) | A kind of wire drawing oil wastewater treatment equipment and its treatment process | |
CN103170160B (en) | Water removal method by utilizing mixed solvent of methylbenzene and 1,2-dimethoxyethane | |
CN217662443U (en) | Be used for industry VOCs exhaust-gas treatment equipment | |
CN209940681U (en) | Reclaimed water ion exchange treatment device | |
CN206219240U (en) | The purified water water flowing out structure of water purifier | |
CN201857039U (en) | Bucket cleaning and oxygen exhausting device | |
CN221544375U (en) | Industrial ultrapure water treatment equipment | |
CN217808996U (en) | Circulating adsorption device for active coke |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
RJ01 | Rejection of invention patent application after publication | ||
RJ01 | Rejection of invention patent application after publication |
Application publication date: 20171103 |