CN1063313C - Wet process for producing calcium hydrophosphate as fodder from phosphoric acid - Google Patents

Wet process for producing calcium hydrophosphate as fodder from phosphoric acid Download PDF

Info

Publication number
CN1063313C
CN1063313C CN95105662A CN95105662A CN1063313C CN 1063313 C CN1063313 C CN 1063313C CN 95105662 A CN95105662 A CN 95105662A CN 95105662 A CN95105662 A CN 95105662A CN 1063313 C CN1063313 C CN 1063313C
Authority
CN
China
Prior art keywords
phosphoric acid
reaction
composite fertilizer
calcium hydrophosphate
compound fertilizer
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.)
Expired - Fee Related
Application number
CN95105662A
Other languages
Chinese (zh)
Other versions
CN1123616A (en
Inventor
朱运泽
吴树威
陈朴
黄德明
贾振宇
周德
谢伟
莫桂英
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
ZHANHUA ENTERPRISES GROUP CO GUANGDONG PROV
Original Assignee
ZHANHUA ENTERPRISES GROUP CO GUANGDONG PROV
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by ZHANHUA ENTERPRISES GROUP CO GUANGDONG PROV filed Critical ZHANHUA ENTERPRISES GROUP CO GUANGDONG PROV
Priority to CN95105662A priority Critical patent/CN1063313C/en
Publication of CN1123616A publication Critical patent/CN1123616A/en
Application granted granted Critical
Publication of CN1063313C publication Critical patent/CN1063313C/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Landscapes

  • Fertilizers (AREA)

Abstract

The present invention relates to a technology for preparing feed-grade calcium hydrophosphate by using wet-process phosphoric acid, which comprises: a reactor is added in a device for producing compound fertilizer; purified phosphoric acid is jetted on reaction material for reaction, and the technological conditions of the reaction are controlled. Thus, the feed-grade calcium hydrophosphate can be generated by the reaction. When compound fertilizer needs to be produced, the technological process of the present invention is converted into a technological process for producing compound fertilizer with an NPK compound fertilizer producing method. Because two kinds of products can be produced by a set of devices, the cost is reduced, and the economic benefit is obviously increased. The technology is suitable for an NPK compound fertilizer device for developing new products, and is also suitable for establishing a set of new producing devices.

Description

Phosphoric acid by wet process is produced the method for calcium hydrophosphate fodder
The invention belongs to a kind of phosphoric acid by wet process and produce the method for calcium hydrophosphate fodder.
At present, with the phosphoric acid by wet process is the raw material production calcium hydrophosphate fodder, the liquid phase flow process that adopts two sections neutralising phosphoric acids of milk of lime is arranged, the dry method flow process that phosphoric acid and calcium carbonate reaction are also arranged all will be built a cover production equipment in addition, and 93110897.7 1 kinds of methods of producing calcium hydrogen phosphate fodder of patent, be to adopt the basis of two sections neutralisations of milk of lime and set up a pretreatment process, not only set up device, improved cost simultaneously, very uneconomical.
The purpose of this invention is to provide a kind of phosphoric acid by wet process and produce the method for calcium hydrophosphate fodder, promptly be in original composite fertilizer production equipment, set up a special reaction device, with concentration is 42% purifying phosphoric acid (through defluorinate, removing heavy metals) and content is that lime carbonate more than 97% is made raw material, produce calcium hydrophosphate fodder, while is production composite fertilizer also, reaches the purpose that a covering device is produced two kinds of products, the also suitable cover secondary calcium phosphate new production device of building of the present invention.
The present invention is in composite fertilizer's production equipment, increases a reactor, purifying phosphoric acid is ejected on the reaction mass reacts, and generates calcium hydrophosphate fodder, in composite fertilizer's preorder production equipment (1), with purity % 〉=97, F%=0.075, heavy metal P 2 b+ %<0.001 lime carbonate mixes with the returning charge that comes from composite fertilizer's postorder production equipment (4), adds in the secondary calcium phosphate reactor (2), comes from the P of composite fertilizer's preorder production equipment (1) 2O 5%=38~43, F%=0.13, heavy metal P 2 bThe purifying phosphoric acid of+%<0.002 is ejected on the reaction mass and reacts, reaction time 30~60 seconds, and returning charge: product: 1~4: 1, CaO/P 2O 5(ore deposit acid ratio): 0.77~0.84, temperature of reaction: 30~70 ℃, make reaction generate secondary calcium phosphate, the slip that comes out is sent to composite fertilizer's postorder device processes, obtains calcium hydrophosphate fodder.When need production composite fertilizer, switch to the technical process of composite fertilizer, press the method production of NPK composite fertilizer.
The present invention is in former composite fertilizer production equipment, increase a reactor, with purifying phosphoric acid be ejected into returning charge blended material on react, the processing condition of control reaction just can be reacted the secondary calcium phosphate that generates feed grade, when needs production composite fertilizer, switch to the compound fertilizer technology flow process, press the method production of NPK composite fertilizer, a set of equipment is produced two kinds of products, and cost is low; Remarkable in economical benefits adapts to the NPK compound fertilizer facility usefulness of developing new product.
Description of drawings:
Fig. 1 is a flow diagram of the present invention.
The present invention increases a reactor in former composite fertilizer production equipment, when need are produced secondary calcium phosphate, switch to the technology circuit of producing secondary calcium phosphate, with purity % 〉=97, F%=0.075, heavy metal P 2 bIn the lime carbonate of+%<0.001 and the composite fertilizer's postorder production equipment, P 2O 5%=42.3, F%=0.12, Ca%=23.6, heavy metal P 2 bThe returning charge of+%<0.002 (secondary calcium phosphate) mixes and adds in the reactor P 2O 5%=38~43, F%=0.13, heavy metal P 2 B+The purifying phosphoric acid of %<0.002 is ejected on the reaction mass and reacts, reaction time 40~50 seconds, returning charge: product preferably 2: 1, CaO/P 2O 5(ore deposit acid than) preferably 0.80, preferably 40 ℃ of temperature of reaction are sent to drying from the work in-process that reactor comes out, by analyzing work in-process free acid and carbonic acid gas, the transformation efficiency of assaying reaction.When needs production composite fertilizer, switch to the technical process of composite fertilizer, press the method production of NPK composite fertilizer, a set of equipment is produced two kinds of products, and cost is low, and suitable NPK compound fertilizer facility is developed new product, and also can suit to build a cover new production device.

Claims (1)

1, a kind of phosphoric acid by wet process is produced the method for calcium hydrophosphate fodder, be in composite fertilizer's production equipment, increase a reactor, purifying phosphoric acid is ejected on the reaction mass reacts, generate calcium hydrophosphate fodder, it is characterized in that: purity % 〉=97, F%=0.075, heavy metal P 2 b+ %<0.001 lime carbonate mixes with the returning charge that comes from composite fertilizer's postorder production equipment (4), adds in the secondary calcium phosphate reactor (2), comes from the P of composite fertilizer's preorder production equipment (1) 2O 5%=38~43, F%=0.13, heavy metal P 2 bThe purifying phosphoric acid of+%<0.002 is ejected on the reaction mass and reacts, reaction time 30~60 seconds, and returning charge: product: 1~4: 1, CaO/P 2O 5(ore deposit acid ratio): 0.77~0.84, temperature of reaction: 30~70 ℃, make reaction generate secondary calcium phosphate, the slip that comes out is sent to composite fertilizer's postorder device processes, obtains calcium hydrophosphate fodder.
CN95105662A 1995-06-26 1995-06-26 Wet process for producing calcium hydrophosphate as fodder from phosphoric acid Expired - Fee Related CN1063313C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN95105662A CN1063313C (en) 1995-06-26 1995-06-26 Wet process for producing calcium hydrophosphate as fodder from phosphoric acid

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN95105662A CN1063313C (en) 1995-06-26 1995-06-26 Wet process for producing calcium hydrophosphate as fodder from phosphoric acid

Publications (2)

Publication Number Publication Date
CN1123616A CN1123616A (en) 1996-06-05
CN1063313C true CN1063313C (en) 2001-03-21

Family

ID=5075564

Family Applications (1)

Application Number Title Priority Date Filing Date
CN95105662A Expired - Fee Related CN1063313C (en) 1995-06-26 1995-06-26 Wet process for producing calcium hydrophosphate as fodder from phosphoric acid

Country Status (1)

Country Link
CN (1) CN1063313C (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102701171B (en) * 2012-06-21 2014-03-19 中化云龙有限公司 Production method of feed-grade granular calcium hydrogen phosphate III-type product

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1091392A (en) * 1993-02-25 1994-08-31 张小平 A kind of method of producing calcium hydrogen phosphate fodder

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1091392A (en) * 1993-02-25 1994-08-31 张小平 A kind of method of producing calcium hydrogen phosphate fodder

Also Published As

Publication number Publication date
CN1123616A (en) 1996-06-05

Similar Documents

Publication Publication Date Title
CN105600763B (en) A kind of method that fluoride salt method of purification produces industrial monoammonium phosphate
CN111086977B (en) Method for preparing MCP and MDCP (Madin-Darby Canine phosphate) by using raffinate acid
EP0093466A1 (en) Process for the preparation of urea
CN1029517C (en) Process and equipment for tower-type wet production of phosphoric acid
CN1063313C (en) Wet process for producing calcium hydrophosphate as fodder from phosphoric acid
CN108569812B (en) Treatment system and treatment method for wastewater containing low-concentration sulfuric acid
CN1174812A (en) Industrial monoammonium phosphate and productive method for industrial monoammunium phosphate and calcium hydrogen phosphate fodder
CN213446251U (en) System for producing solid carbonate
CN1058005A (en) Method with preparing high-purity technical calcium carbonate from calcium carbide dregs
CN116281910A (en) Method for preparing feed-grade calcium hydrophosphate by utilizing wet method to purify phosphoric acid byproduct
EG20972A (en) Process and plant for the production of urea with high conversion yield and low energy consumption
CN110316747A (en) A method of synthetical recovery lithium and phosphorus from lithium phosphate
CN212864145U (en) Phosphoric acid dearsenification system
CN210595277U (en) System for utilize synthetic ammonia gas-liquid separation's aqueous ammonia production monoammonium phosphate
CN1064334C (en) Art for phosphoric ore secondary decomposition by using extracted phosphoric acid
CN210885316U (en) Stable and efficient wet-process phosphoric acid production system
CN210710760U (en) System for producing caprolactam from caprolactam sulfate and feed-grade calcium hydrophosphate
CN112194110A (en) Method for preparing industrial-grade potassium dihydrogen phosphate
CN212476117U (en) Device for producing industrial-grade potassium dihydrogen phosphate from wet-process phosphoric acid residues
CN108328590A (en) The method for preparing synthos co-production industrial monoammonium phosphate
CN111515215B (en) Harmless treatment method for n-butyl thiophosphoric triamide hazardous waste
CN85102377A (en) With phosphorus ore, sylvite method of fractional steps potassium dihydrogen phosphate making
CN112225228B (en) Method and system for preparing ammonium sulfate by using cement kiln tail waste gas and phosphogypsum
CN118458916A (en) Recovery process for zero emission of ammonium sulfate waste liquid in enzyme preparation industry
SU1326552A1 (en) Method of producing ammonium fluoride

Legal Events

Date Code Title Description
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C06 Publication
PB01 Publication
C14 Grant of patent or utility model
GR01 Patent grant
C19 Lapse of patent right due to non-payment of the annual fee
CF01 Termination of patent right due to non-payment of annual fee