CN203976423U - A kind of sodium wolframate retrieving arrangement for the right ammonium salt production line of left phosphorus - Google Patents

A kind of sodium wolframate retrieving arrangement for the right ammonium salt production line of left phosphorus Download PDF

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Publication number
CN203976423U
CN203976423U CN201420446992.6U CN201420446992U CN203976423U CN 203976423 U CN203976423 U CN 203976423U CN 201420446992 U CN201420446992 U CN 201420446992U CN 203976423 U CN203976423 U CN 203976423U
Authority
CN
China
Prior art keywords
group
withdrawing
sodium wolframate
resin
retrieving arrangement
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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 - Fee Related
Application number
CN201420446992.6U
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Chinese (zh)
Inventor
许友兵
张华锋
王浩
丁勇
李斌
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SHAYANG QINJIANG CHEMICAL Co Ltd
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SHAYANG QINJIANG CHEMICAL Co Ltd
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Priority to CN201420446992.6U priority Critical patent/CN203976423U/en
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Publication of CN203976423U publication Critical patent/CN203976423U/en
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Expired - Fee Related legal-status Critical Current

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Abstract

A kind of sodium wolframate retrieving arrangement for the right ammonium salt production line of left phosphorus, it also has sodium wolframate retrieving arrangement, sodium wolframate retrieving arrangement comprises one group of withdrawing can (3), one group of resin (4) and one group of sieve plate (5), one group of sieve plate (5) is arranged on respectively in one group of withdrawing can (3), and be positioned at below material taking mouth (3-1), one group of resin (4) is positioned on one group of sieve plate (5), the opening for feed of one group of withdrawing can (3) communicates with the hole on pipeline (1-1) respectively, oxidizing and crystallizing still has opening for feed on (2), the outlet of one group of withdrawing can (3) is by the feeding inlet on pipeline and oxidizing and crystallizing still (2), the inlet and outlet of one group of withdrawing can (3) is respectively equipped with valve.The utility model advantage is: this device is simple to be used, and utilizes resin to reclaim sodium wolframate, and each recovery can be reclaimed the sodium wolframate of 8-10KG, and it is utilized again, has reduced production cost.

Description

A kind of sodium wolframate retrieving arrangement for the right ammonium salt production line of left phosphorus
Technical field
The utility model relates to the right ammonium salt production line of left phosphorus field, is specifically related to a kind of sodium wolframate retrieving arrangement for the right ammonium salt production line of left phosphorus.
Background technology
?at present, enter in oxidizing and crystallizing still, need to add sodium wolframate on the right ammonium salt production line of left phosphorus from stills for air blowing, and the high per kilogram price of existing sodium wolframate price needs 168 yuan, sodium wolframate, using later just directly discharge, is not recycled, and wastes resource.
Utility model content
The purpose of this utility model is exactly in oxidizing and crystallizing still, to need to add sodium wolframate for entering to from stills for air blowing on the right ammonium salt production line of left phosphorus at present, and the high per kilogram price of existing sodium wolframate price needs 168 yuan, sodium wolframate is using later just directly discharge, be not recycled, the deficiency of waste resource, and a kind of sodium wolframate retrieving arrangement for the right ammonium salt production line of left phosphorus is provided.
The utility model comprises stills for air blowing and the oxidizing and crystallizing still of the right ammonium salt production line of left phosphorus, the discharge port of stills for air blowing is by the feeding inlet of pipeline and oxidizing and crystallizing still, it is characterized in that it also has sodium wolframate retrieving arrangement, sodium wolframate retrieving arrangement comprises one group of withdrawing can, one group of resin and one group of sieve plate, on pipeline, have discharge hole, on one group of withdrawing can, have material taking mouth, one group of sieve plate is arranged on respectively in one group of withdrawing can, and be positioned at below material taking mouth, one group of resin is positioned on one group of sieve plate, the opening for feed of one group of withdrawing can communicates with the hole on pipeline respectively, on oxidizing and crystallizing still, have opening for feed, the outlet of one group of withdrawing can is by the feeding inlet on pipeline and oxidizing and crystallizing still, the inlet and outlet of one group of withdrawing can is respectively equipped with valve.
Resin is D354 particulate resins.
The volume of resin is greater than the diameter in the hole on sieve plate.
The utility model advantage is: this device is simple to be used, and utilizes resin to reclaim sodium wolframate, and each recovery can be reclaimed the sodium wolframate of 8-10KG, and it is utilized again, has reduced production cost.
brief description of the drawings
Fig. 1 is the utility model structural representation.
Embodiment
As shown in Figure 1, the utility model comprises stills for air blowing 1 and the oxidizing and crystallizing still 2 of the right ammonium salt production line of left phosphorus, the discharge port of stills for air blowing 1 is by the feeding inlet of pipeline 1-1 and oxidizing and crystallizing still 2, it is characterized in that it also has sodium wolframate retrieving arrangement, sodium wolframate retrieving arrangement comprises one group of withdrawing can 3, one group of resin 4 and one group of sieve plate 5, on pipeline 1-1, have discharge hole, on one group of withdrawing can 3, have material taking mouth 3-1, one group of sieve plate 5 is arranged on respectively in one group of withdrawing can 3, and be positioned at below material taking mouth 3-1, one group of resin 4 is positioned on one group of sieve plate 5, the opening for feed of one group of withdrawing can 3 communicates with the hole on pipeline 1-1 respectively, on oxidizing and crystallizing still 2, have opening for feed, the outlet of one group of withdrawing can 3 is by the feeding inlet on pipeline and oxidizing and crystallizing still 2, the inlet and outlet of one group of withdrawing can 3 is respectively equipped with valve.
Resin is D354 particulate resins.
The volume of resin is greater than the diameter in the hole on sieve plate 5.
Use-pattern: when the oxidation first product of the right ammonium salt of left phosphorus enters to stills for air blowing 1 when interior, in stills for air blowing 1, add sodium wolframate, the oxidation first product completing when oxidation is in the time carrying by pipeline that respectively to one, group withdrawing can 3 was interior, one group of interior unnecessary not complete reaction sodium wolframate of withdrawing can 3 is adsorbed on resin 4, the oxidation first product of the right ammonium salt of left phosphorus continues to flow in oxidizing and crystallizing still 2, timing is taken out resin from the material taking mouth 3-1 of one group of withdrawing can 3, has the resin of sodium wolframate to be fed in stills for air blowing 1 absorption again and again reacts with oxidation first product.

Claims (1)

1. the sodium wolframate retrieving arrangement for the right ammonium salt production line of left phosphorus, it comprises stills for air blowing (1) and the oxidizing and crystallizing still (2) of the right ammonium salt production line of left phosphorus, the discharge port of stills for air blowing (1) is the feeding inlet with oxidizing and crystallizing still (2) by pipeline (1-1), it is characterized in that it also has sodium wolframate retrieving arrangement, sodium wolframate retrieving arrangement comprises one group of withdrawing can (3), one group of resin (4) and one group of sieve plate (5), on pipeline (1-1), have discharge hole, on one group of withdrawing can (3), have material taking mouth (3-1), one group of sieve plate (5) is arranged on respectively in one group of withdrawing can (3), and be positioned at below material taking mouth (3-1), one group of resin (4) is positioned on one group of sieve plate (5), the opening for feed of one group of withdrawing can (3) communicates with the hole on pipeline (1-1) respectively, oxidizing and crystallizing still has opening for feed on (2), the outlet of one group of withdrawing can (3) is by the feeding inlet on pipeline and oxidizing and crystallizing still (2), the inlet and outlet of one group of withdrawing can (3) is respectively equipped with valve, resin is D354 particulate resins, the volume of resin is greater than the diameter in the hole on sieve plate (5).
CN201420446992.6U 2014-08-11 2014-08-11 A kind of sodium wolframate retrieving arrangement for the right ammonium salt production line of left phosphorus Expired - Fee Related CN203976423U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201420446992.6U CN203976423U (en) 2014-08-11 2014-08-11 A kind of sodium wolframate retrieving arrangement for the right ammonium salt production line of left phosphorus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201420446992.6U CN203976423U (en) 2014-08-11 2014-08-11 A kind of sodium wolframate retrieving arrangement for the right ammonium salt production line of left phosphorus

Publications (1)

Publication Number Publication Date
CN203976423U true CN203976423U (en) 2014-12-03

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN201420446992.6U Expired - Fee Related CN203976423U (en) 2014-08-11 2014-08-11 A kind of sodium wolframate retrieving arrangement for the right ammonium salt production line of left phosphorus

Country Status (1)

Country Link
CN (1) CN203976423U (en)

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C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20141203

Termination date: 20190811