NOVELTY - A glyphosate continuous production device contains synthesis kettle (1) through bottom conveying pipe and condensation tower (2) is connected to top end of mixer in which condensation tower through conveying pipe and circulation pump is connected to front end of mixer (4) , mixer is set with upper end of high hydrochloric acid storage tank (18), mixer by end of conveying pipe is connected to circulation pump, circulation pump and circuit pipeline is connected to top end of mixing reaction kettle (5), and top end of alkali washing tower (9) is connected to lower part of methylal tower (10).    USE - A glyphosate continuous production device (claimed).    ADVANTAGE - Product increases chloride content and product yield, reduces energy consumption, and has good environmental protection.    DETAILED DESCRIPTION - A glyphosate continuous production device contains synthesis kettle (1) through bottom conveying pipe and condensation tower (2) is connected to top end of mixer in which condensation tower through conveying pipe and circulation pump is connected to front end of mixer (4), mixer is set with upper end of high hydrochloric acid storage tank (18), mixer by end of conveying pipe is connected to circulation pump, circulation pump and circuit pipeline is connected to top end of mixing reaction kettle (5), mixing reaction kettle through conveying pipe and force pump (6) is connected to multi-level balance grooves (7-1,7-2,7-3), multi-level balance grooves through conveying pipe is connected to top of multi-stage deacidifying kettles (8-1,8-2,8-3), multi-stage deacidifying kettles through end of converging circuit pipeline is connected to lower part of alkali washing tower (9), top end of alkali washing tower through circuit pipeline is connected to lower part of methylal tower (10), top end of methylal tower through circuit pipeline is connected to 1st condenser (11-1), lower end of 1st condenser and 1st gas-liquid separator (14-1) are connected, upper part of 1st gas-liquid separator and bottom of methylal storage tank (12) are connected, methyl alcohol tower (13) through conveying pipe and 2nd condenser (11-2) is connected, and bottom of 2nd condenser is connected to 2nd gas-liquid separator (14-2). An INDEPENDENT CLAIM is included for continuous production of glyphosate which involves feeding methanol and ethylenediamine into synthesis kettle by conveying pipe, contacting inner input of aminoacetic acid and paraformaldehyde, performing addition reaction to obtain reaction liquid, preserving heat of reaction liquid in conveying pipeline and feeding to condensation kettle mixer, subjecting mixer of condensation kettle and top end input of condensation kettle into condensation reaction, placing condensate into heat preservation pipeline and high hydrochloric acid tank (18) and feeding into mixer (4) to mix uniformly, placing mixed into hydrolyzing reaction kettle, obtaining hydrolyzate, placing hydrolyzate through magnetic pump into balance groove (7-1,7-2,7-3) via balance groove pressure equalizing, placing hydrolyzate into acidifying kettle, obtaining glyphosate solid and acid tail gas, processing glyphosate solid, discharging, crystallizing, drying, packing, introducing deacidification tail gas into alkali washing tower (9) and removing acid gas, feeding removed tail acid gas from alkali washing tower into top part input methylal, introducing tail gas into 2-level condenser methylal fraction tower, sending condensed tail gas into gas-liquid separator, entering condensation liquid from gas-liquid separator into separate methylal storage tank (12), feeding tail gas into methyl alcohol tower (13), entering tail gas into 2-level condenser to condense methanol tower fraction, putting condensed tail condensation gas to methyl chloride recovery system, and introducing condensation liquid into methyl alcohol storage tank (15).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of glyphosate continuous production device.    Synthesis kettle (1)    Condensation tower (2)    Mixer (4)    Mixing reaction kettle (5)    Force pump (6)    Multi-level balance grooves (7-1,7-2,7-3)    Multi-stage deacidifying kettles (8-1,8-2,8-3)    Alkali washing tower (9)    Methylal tower (10)    1st condenser (11-1)    2nd condenser (11-2)    Methylal storage tank (12)    Methyl alcohol tower (13)    1st gas-liquid separator (14-1)    2nd gas-liquid separator (14-2)    Methyl alcohol storage tank (15)    High hydrochloric acid storage tank (18)