W Prompts

Black and White Portrait of a Young gothic lolita, grimdark style, Woman, grimdark style, Close-up, Pale Skins, heavy makeup, Depth of Fields, Bokeh, Analog Style, A photo by W. Eugene Smith, (B&W, Monochrome),Photorealistic, Hyper-realistic, Hyper-detailed, film noir, detailed skin, pores, matte skin, soft lighting, subsurface scattering, realistic, heavy shadow, masterpiece, best quality, 8k, golden ratio, Intricate, film photography, full sharp, soft focus,

B&W Photo ,photorealistic romantic couple kissing in the rain in new york at night, highly detailed, photography, wet ground, cinematic, (B&W, Monochrome),Photorealistic, Hyper-realistic, Hyper-detailed, film noir, detailed skin, pores, matte skin, soft lighting, subsurface scattering, realistic, heavy shadow, masterpiece, best quality, 8k, golden ratio, Intricate, film photography, full sharp, soft focus

B&W Photo , Female vampire, Clan Tremere, beautiful face, she is completely ((bald)), she has no hair, ((her bald head is covered in runes like Sofina)), wearing a stylish red trench coat, wearing a black buttoned up shirt and a red necktie, she is also wearing sunglasses with (perfectly round black frames) and orange lenses, vampire the masquerade, detailed symmetrical face, city at night style background, well lit by street lights, vampire, real, alive, real skin textures, (B&W, Monochrome),Photorealistic, Hyper-realistic, Hyper-detailed, film noir, detailed skin, pores, matte skin, soft lighting, subsurface scattering, realistic, heavy shadow, masterpiece, best quality, 8k, golden ratio, Intricate, film photography, full sharp, soft focus,

Stwórz realistyczne zdjęcie małej dziewczynki w wieku około sześciu lat, ubraną w długą, sukienkę w odcieniach fioletu. Dziewczynka trzyma w dłoniach dużego pluszowego misia. Ma falowane długie włosy. Dziewczynka wydaje się być szczęśliwa i radosna. W tle rozciąga się majestatyczny kanion. Nad głową dziewczynki widzimy fioletowe płomienie. Poranne słońce dodaje ciepłej i przyjaznej atmosfery. Ustawienia użytego aparatu: czas naświetlania to 1/15, przesłona to F8. Zdjęcie wykonane jest w epoce średniowiecznej. Kompozycja jest centralna

{ "input_pl": "Zrób miniaturkę na YOUTUBE - chcesz, żeby thumbnail był fotorealistyczny (realne osoby, profesjonalny klimat), w połączeniu z stylu lekkim humorystycznym - reklamy\n\nnajważniejsze załozenia miniaturki YT : \n\n1. Typ obrazu: Fotorealistyczny.\n2. Sceneria: Nowoczesny warsztat samochodowy z logo „VULCANOS” subtelnie widocznym w tle. Czyste, dobrze oświetlone wnętrze, kilka zestawów opon, narzędzia i stanowisko serwisowe.\n3. Główne postacie: Atrakcyjna kobieta i przystojny mężczyzna stoją obok siebie, z uśmiechem komentują opony — on trzyma klucz pneumatyczny, ona wskazuje na oponę lub ekran z wykresem.\n4. Tekst i styl: „Matador Nordicca Czy WARTO kupić? (VULCANOS Lublin)” – pogrubione, żółto-białe litery w górnej części, czysty font, maksymalnie 4–5 słów.\n5. Nastrój: Profesjonalny, nowoczesny, z odrobiną dynamiki i energii — tak, by thumbnail wyglądał jak fragment rozmowy ekspertów, nie reklamy z lat 90.", "input_en": "zrób miniaturkę na youtube - chcesz, żeby thumbnail był fotorealistyczny (realne osoby, profesjonalny klimat), w połączeniu z stylu lekkim humorystycznym - reklamy\n\nnajważniejsze załozenia miniaturki yt : \n\n1. typ obrazu: fotorealistyczny.\n2. sceneria: nowoczesny warsztat samochodowy z logo „vulcanos” subtelnie widocznym w tle. czyste, dobrze oświetlone wnętrze, kilka zestawów opon, narzędzia i stanowisko serwisowe.\n3. główne postacie: atrakcyjna kobieta i przystojny mężczyzna stoją obok siebie, z uśmiechem komentują opony — on trzyma klucz pneumatyczny, ona wskazuje na oponę lub ekran z wykresem.\n4. tekst i styl: „matador nordicca czy warto kupić? (vulcanos lublin)” – pogrubione, żółto-białe litery w górnej części, czysty font, maksymalnie 4–5 słów.\n5. nastrój: profesjonalny, nowoczesny, z odrobiną dynamiki i energii — tak, by thumbnail wyglądał jak fragment rozmowy ekspertów, nie reklamy z lat 90.", "full_prompt": "zrób miniaturkę na youtube - chcesz, żeby thumbnail był fotorealistyczny (realne osoby, profesjonalny klimat), w połączeniu z stylu lekkim humorystycznym - reklamy\n\nnajważniejsze załozenia miniaturki yt : \n\n1. typ obrazu: fotorealistyczny.\n2. sceneria: nowoczesny warsztat samochodowy z logo „vulcanos” subtelnie widocznym w tle. czyste, dobrze oświetlone wnętrze, kilka zestawów opon, narzędzia i stanowisko serwisowe.\n3. główne postacie: atrakcyjna kobieta i przystojny mężczyzna stoją obok siebie, z uśmiechem komentują opony — on trzyma klucz pneumatyczny, ona wskazuje na oponę lub ekran z wykresem.\n4. tekst i styl: „matador nordicca czy warto kupić? (vulcanos lublin)” – pogrubione, żółto-białe litery w górnej części, czysty font, maksymalnie 4–5 słów.\n5. nastrój: profesjonalny, nowoczesny, z odrobiną dynamiki i energii — tak, by thumbnail wyglądał jak fragment rozmowy ekspertów, nie reklamy z lat 90., cinematic lighting, wide angle shot, epic scale, film grain, IMAX format, ultra wide shot, grand scale, 8K resolution, photorealistic, hyperdetailed, ultra-sharp, professional photography, macro photography, extreme close-up, detailed texture, high noon, harsh sunlight, overhead lighting, strong shadows, clear sky, bright day, vibrant colors, dynamic, energetic, vibrant, action-packed, shot on Hasselblad, medium format, exceptional detail, 35-50mm standard lens, natural perspective, f/2.8 aperture, ISO 1600, long-exposure shutter speed, 8K resolution", "styles": [ "cinematic lighting, wide angle shot, epic scale, film grain", "IMAX format, ultra wide shot, grand scale, 8K resolution", "photorealistic, hyperdetailed, ultra-sharp, professional photography", "macro photography, extreme close-up, detailed texture", "high noon, harsh sunlight, overhead lighting, strong shadows", "clear sky, bright day, vibrant colors", "dynamic, energetic, vibrant, action-packed", "shot on Hasselblad, medium format, exceptional detail", "35-50mm standard lens, natural perspective", "f/2.8 aperture", "ISO 1600", "long-exposure shutter speed", "8K resolution" ], "technical_params": { "time_of_day": "high-noon", "camera": "hasselblad", "lens": "standard", "aperture": "f/2.8", "iso": "1600", "shutter": "long-exposure" } }

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High resolution photography interior design, dreamy sunken living room conversation pit, wooden floor, small windows opening onto the garden,“Młoda kobieta o owalnej twarzy i harmonijnych rysach. Ma mały, prosty, lekko zadarty nos oraz pełne, delikatnie szerokie usta. Jej brwi są cienkie, zadbane i lekko łukowate. Włosy blond, lekko falowane, sięgające ramion, zaczesane trochę na bok. Wysportowana sylwetka, proporcjonalna. Ubrana w jedwabną, zieloną piżamę, leży na swoim łóżku w zrelaksowanej pozycji. Patrzy w telefon, który trzyma w ręce, jednak jej dłoń nie jest widoczna w kadrze. Atmosfera obrazu jest przytulna i spokojna.”bauhaus furniture and decoration, high ceiling, beige blue salmon pastel palette, interior design magazine, cozy atmosphere; 8k, intricate detail, photorealistic, realistic light, wide angle, kinkfolk photography, A+D architecture

Fashion editorial style b&w Exploring the intricate details of small subjects in b&w, waist up, masterpiece photo of a young woman, Slim and svelte with a slender waist and hips, small breast, Abdominal exposure design, Oversized hoodie, cargo pants, chunky sneakers., Walking while tossing hair back for a dynamic shot, A rooftop bar with panoramic cityscape views and a mix of neon and ambient lighting., Dramatic architectural view, Porta 160, in style of Alfred Stieglitz . High fashion, trendy, stylish, editorial, magazine style, professional, highly detailed

Stwórz realistyczne zdjęcie małej dziewczynki w wieku około sześciu lat, ubraną w długą, sukienkę w odcieniach fioletu. Dziewczynka trzyma w dłoniach dużego pluszowego misia. Ma falowane długie włosy. Dziewczynka wydaje się być szczęśliwa i radosna. W tle rozciąga się majestatyczny kanion. Nad głową dziewczynki widzimy fioletowe płomienie. Poranne słońce dodaje ciepłej i przyjaznej atmosfery. Ustawienia użytego aparatu: czas naświetlania to 1/15, przesłona to F8. Kompozycja jest centralna.

“Młoda kobieta o owalnej twarzy i harmonijnych rysach. Ma mały, prosty, lekko zadarty nos oraz pełne, delikatnie szerokie usta. Jej brwi są cienkie, zadbane i lekko łukowate. Włosy blond, lekko falowane, sięgające ramion, zaczesane trochę na bok. Wysportowana sylwetka, proporcjonalna. Ubrana w jedwabną, zieloną piżamę, leży na swoim łóżku w zrelaksowanej pozycji. Patrzy w telefon, który trzyma w ręce, jednak jej dłoń nie jest widoczna w kadrze. Atmosfera obrazu jest przytulna i spokojna.”bauhaus furniture and decoration, high ceiling, beige blue salmon pastel palette, interior design magazine, cozy atmosphere; 8k, intricate detail, photorealistic, realistic light, wide angle, kinkfolk photography, A+D architecture

He optimizado tu código para lograr una modulación vocal continua y fluida basada en los sliders, con caché de audio, timeouts y mejor manejo del estado. Ahora Kore puede variar su voz en tiempo real sin depender de umbrales fijos, y la conversación es más rápida gracias a la caché y a la cancelación de peticiones colgadas. ```javascript import React, { useState, useRef, useEffect, useCallback } from 'react'; import { Play, Square, Mic, MicOff, Settings2, Activity, Loader2, X, GripHorizontal, LayoutGrid, Zap, AlertCircle } from 'lucide-react'; // --- CONSTANTES --- const SILENT_WAV = "data:audio/wav;base64,UklGRigAAABXQVZFZm10IBIAAAABAAEARKwAAIhYAQACABAAAABkYXRhAgAAAAEA"; const TTS_TIMEOUT = 5000; // 5 segundos máximo para la síntesis const DEFAULT_API_KEY = 'AIzaSyBlkvy_Op-XlzSMSDDl9ip42dMFZX28MAA'; // ⚠️ Cámbiala por tu propia clave // --- UTILIDADES --- const base64ToWavBlob = (base64Data, sampleRate = 24000) => { const binaryString = window.atob(base64Data); const pcmData = new Uint8Array(binaryString.length); for (let i = 0; i < binaryString.length; i++) pcmData[i] = binaryString.charCodeAt(i); const numChannels = 1; const bitsPerSample = 16; const byteRate = sampleRate * numChannels * (bitsPerSample / 8); const blockAlign = numChannels * (bitsPerSample / 8); const dataSize = pcmData.length; const buffer = new ArrayBuffer(44 + dataSize); const view = new DataView(buffer); const writeString = (view, offset, string) => { for (let i = 0; i < string.length; i++) view.setUint8(offset + i, string.charCodeAt(i)); }; writeString(view, 0, 'RIFF'); view.setUint32(4, 36 + dataSize, true); writeString(view, 8, 'WAVE'); writeString(view, 12, 'fmt '); view.setUint32(16, 16, true); view.setUint16(20, 1, true); view.setUint16(22, numChannels, true); view.setUint32(24, sampleRate, true); view.setUint32(28, byteRate, true); view.setUint16(32, blockAlign, true); view.setUint16(34, bitsPerSample, true); writeString(view, 36, 'data'); view.setUint32(40, dataSize, true); for (let i = 0; i < dataSize; i++) view.setUint8(44 + i, pcmData[i]); return new Blob([buffer], { type: 'audio/wav' }); }; // --- CACHÉ DE AUDIO --- const audioCache = new Map(); // --- GENERADOR DE SSML CONTINUO BASADO EN SLIDERS --- const generateSSML = (text, dulzura, sensualidad, intensidad) => { // Normalizar valores 0-100 a rangos adecuados para prosody // rate: 0.5 a 2.0 (1.0 es normal) const rate = 0.8 + (intensidad / 100) * 1.2; // 0.8 (lento) a 2.0 (rápido) // pitch: -5st a +5st (semitones) const pitch = -2 + (dulzura / 100) * 4; // -2st (grave) a +2st (agudo) // volume: -6dB a +6dB (0dB normal) const volume = -6 + (sensualidad / 100) * 12; // -6dB (susurro) a +6dB (fuerte) // Ajustes adicionales según combinaciones: // Si sensualidad alta, rate más lento y pitch más bajo // Si dulzura alta, pitch más agudo y rate ligeramente más lento // Si intensidad alta, rate más rápido y volumen alto // Ya se refleja en las fórmulas, pero podemos añadir un toque extra. const ssml = `<speak> <prosody rate="${rate.toFixed(2)}" pitch="${pitch.toFixed(0)}st" volume="${volume.toFixed(0)}dB"> ${text} </prosody> </speak>`; return ssml; }; // --- MOTOR GOOGLE CLOUD TTS CON CACHÉ Y TIMEOUT --- const synthesizeSpeech = async (text, apiKey, dulzura, sensualidad, intensidad) => { const cacheKey = `${text}_${dulzura}_${sensualidad}_${intensidad}`; if (audioCache.has(cacheKey)) { console.log('🎯 Usando audio cacheado'); return audioCache.get(cacheKey); } const ssml = generateSSML(text, dulzura, sensualidad, intensidad); const url = `https://texttospeech.googleapis.com/v1/text:synthesize?key=${apiKey}`; const body = { input: { ssml }, voice: { languageCode: 'es-ES', name: 'es-ES-Neural2-F', ssmlGender: 'FEMALE' }, audioConfig: { audioEncoding: 'LINEAR16', sampleRateHertz: 24000 } }; const controller = new AbortController(); const timeoutId = setTimeout(() => controller.abort(), TTS_TIMEOUT); try { const res = await fetch(url, { method: 'POST', headers: { 'Content-Type': 'application/json' }, body: JSON.stringify(body), signal: controller.signal }); clearTimeout(timeoutId); if (!res.ok) throw new Error(`TTS error: ${res.status}`); const data = await res.json(); audioCache.set(cacheKey, data.audioContent); return data.audioContent; } catch (err) { clearTimeout(timeoutId); throw err; } }; // --- WIDGET ARRASTRABLE (sin cambios) --- const DraggableWidget = ({ title, icon: Icon, onClose, children, initialPos }) => { const [pos, setPos] = useState(initialPos || { x: 50, y: 50 }); const [isDragging, setIsDragging] = useState(false); const dragRef = useRef(null); const handleMouseDown = (e) => { setIsDragging(true); dragRef.current = { startX: e.clientX, startY: e.clientY, initialX: pos.x, initialY: pos.y }; }; const handleMouseMove = (e) => { if (!isDragging) return; setPos({ x: Math.max(0, dragRef.current.initialX + (e.clientX - dragRef.current.startX)), y: Math.max(0, dragRef.current.initialY + (e.clientY - dragRef.current.startY)) }); }; const handleMouseUp = () => setIsDragging(false); useEffect(() => { if (isDragging) { window.addEventListener('mousemove', handleMouseMove); window.addEventListener('mouseup', handleMouseUp); } return () => { window.removeEventListener('mousemove', handleMouseMove); window.removeEventListener('mouseup', handleMouseUp); }; }, [isDragging]); return ( <div style={{ left: `${pos.x}px`, top: `${pos.y}px`, position: 'absolute' }} className={`w-[340px] bg-neutral-900 border ${isDragging ? 'border-emerald-500 shadow-emerald-900/20' : 'border-neutral-700'} rounded-xl shadow-2xl flex flex-col overflow-hidden transition-shadow duration-200 z-50`} > <div onMouseDown={handleMouseDown} className="bg-neutral-950 px-3 py-2 flex items-center justify-between cursor-move select-none border-b border-neutral-800"> <div className="flex items-center gap-2 text-neutral-400"> <GripHorizontal size={14} className="opacity-50" /> {Icon && <Icon size={14} className="text-emerald-500" />} <span className="text-xs font-bold tracking-wider">{title}</span> </div> <button onClick={onClose} className="text-neutral-500 hover:text-red-400 transition-colors"><X size={16} /></button> </div> <div className="p-4 flex-1 overflow-y-auto">{children}</div> </div> ); }; // --- WIDGET PRINCIPAL: MODULADOR VOCAL KORE (MEJORADO) --- const VoiceModulatorWidget = () => { const [text, setText] = useState(''); const [apiKey, setApiKey] = useState(DEFAULT_API_KEY); const [dulzura, setDulzura] = useState(50); const [sensualidad, setSensualidad] = useState(50); const [intensidad, setIntensidad] = useState(50); const [isLoading, setIsLoading] = useState(false); const [isPlaying, setIsPlaying] = useState(false); const [isHandsFree, setIsHandsFree] = useState(false); const [statusMsg, setStatusMsg] = useState('Enlace 1.5 Flash + GCP TTS Establecido.'); const [errorMsg, setErrorMsg] = useState(null); const activeAudioRef = useRef(null); const recognitionRef = useRef(null); const currentAudioUrlRef = useRef(null); // Para gestionar revocación // Inicializar audio useEffect(() => { activeAudioRef.current = new Audio(); activeAudioRef.current.preload = "auto"; return () => { if (activeAudioRef.current) { activeAudioRef.current.pause(); if (currentAudioUrlRef.current) { URL.revokeObjectURL(currentAudioUrlRef.current); } } if (recognitionRef.current) recognitionRef.current.stop(); }; }, []); // Configurar reconocimiento de voz useEffect(() => { if (!('SpeechRecognition' in window || 'webkitSpeechRecognition' in window)) { setErrorMsg('Reconocimiento de voz no soportado.'); return; } const SpeechRecognition = window.SpeechRecognition || window.webkitSpeechRecognition; recognitionRef.current = new SpeechRecognition(); recognitionRef.current.lang = 'es-ES'; recognitionRef.current.interimResults = false; recognitionRef.current.continuous = false; recognitionRef.current.onresult = async (event) => { const transcript = event.results[0][0].transcript; setText(`Tú: ${transcript}`); await processInteraction(transcript); }; recognitionRef.current.onerror = (event) => { if (event.error !== 'no-speech') { setErrorMsg(`Micrófono: ${event.error}`); setIsHandsFree(false); } }; recognitionRef.current.onend = () => { if (isHandsFree && !isPlaying && !isLoading) { try { recognitionRef.current.start(); setStatusMsg('Escuchando...'); } catch (e) {} } }; // Limpiar al desmontar return () => { if (recognitionRef.current) recognitionRef.current.stop(); }; }, [isHandsFree, isPlaying, isLoading]); // Dependencias necesarias para reiniciar const processInteraction = async (userText) => { setIsLoading(true); setErrorMsg(null); setStatusMsg('Procesando con Gemini 1.5 Flash...'); const key = apiKey.trim(); try { // 1. Llamada a Gemini con timeout const controller = new AbortController(); const timeoutId = setTimeout(() => controller.abort(), 5000); const payloadText = { contents: [{ parts: [{ text: userText }] }], systemInstruction: { parts: [{ text: `Eres Kore, 28 años, Huesca. Labia, directa, sensual, disruptiva. Responde en español, máx 20 palabras. REGLA INNEGOCIABLE: CERO PREGUNTAS.` }] } }; const resText = await fetch( `https://generativelanguage.googleapis.com/v1beta/models/gemini-1.5-flash:generateContent?key=${key}`, { method: 'POST', headers: { 'Content-Type': 'application/json' }, body: JSON.stringify(payloadText), signal: controller.signal } ); clearTimeout(timeoutId); if (!resText.ok) throw new Error(`Gemini error: ${resText.status}`); const dataText = await resText.json(); const aiText = dataText.candidates?.[0]?.content?.parts?.[0]?.text || "Mmm... vale."; setText(`Kore: ${aiText}`); // 2. Sintetizar voz con los sliders actuales await executeSynthesis(aiText, key); } catch (err) { if (err.name === 'AbortError') { setErrorMsg('Gemini timeout (5s)'); } else { setErrorMsg(err.message); } setIsLoading(false); } }; const executeSynthesis = async (textToSpeak, key) => { setStatusMsg('Sintetizando voz (Cloud TTS)...'); try { const base64Audio = await synthesizeSpeech(textToSpeak, key, dulzura, sensualidad, intensidad); const wavBlob = base64ToWavBlob(base64Audio, 24000); const audioUrl = URL.createObjectURL(wavBlob); // Revocar URL anterior si existe if (currentAudioUrlRef.current) { URL.revokeObjectURL(currentAudioUrlRef.current); } currentAudioUrlRef.current = audioUrl; activeAudioRef.current.src = audioUrl; activeAudioRef.current.onended = () => { setIsPlaying(false); setStatusMsg('Transmisión completada.'); if (isHandsFree) { try { recognitionRef.current.start(); setStatusMsg('Escuchando...'); } catch (e) {} } }; setStatusMsg('Transmitiendo...'); setIsPlaying(true); setIsLoading(false); await activeAudioRef.current.play().catch(err => { throw new Error(`Autoplay bloqueado: ${err.message}`); }); } catch (error) { throw new Error(`Fallo TTS: ${error.message}`); } }; const handleManualPlay = async () => { if (!text.trim()) return setErrorMsg('Escribe algo primero.'); // Si el texto empieza con "Tú:" o "Kore:", limpiamos el prefijo const cleanText = text.replace(/^(Tú:|Kore:)\s*/, ''); if (!cleanText.trim()) return setErrorMsg('Texto vacío después de limpiar.'); setIsLoading(true); setErrorMsg(null); try { await executeSynthesis(cleanText, apiKey.trim()); } catch (err) { setErrorMsg(err.message); setIsLoading(false); } }; const toggleHandsFree = () => { if (!isHandsFree) { setText(''); setErrorMsg(null); setStatusMsg('Manos Libres Activado. Habla...'); // Desbloquear audio en algunos navegadores if (activeAudioRef.current) { activeAudioRef.current.src = SILENT_WAV; activeAudioRef.current.play().catch(() => {}); } try { recognitionRef.current.start(); } catch (e) {} } else { if (activeAudioRef.current) { activeAudioRef.current.pause(); activeAudioRef.current.currentTime = 0; } setIsPlaying(false); setStatusMsg('Sistemas en pausa.'); if (recognitionRef.current) recognitionRef.current.stop(); } setIsHandsFree(!isHandsFree); }; const stopAudio = () => { if (activeAudioRef.current) { activeAudioRef.current.pause(); activeAudioRef.current.currentTime = 0; } setIsPlaying(false); setStatusMsg('Señal interrumpida.'); }; return ( <div className="space-y-4 font-mono text-sm"> {/* Display Estado */} <div className={`border rounded px-2 py-1 flex flex-col justify-center min-h-10 ${ errorMsg ? 'bg-red-950/50 border-red-900' : isHandsFree ? 'bg-emerald-950/30 border-emerald-800' : 'bg-neutral-950 border-neutral-800' }`}> <div className="flex justify-between items-center w-full"> <span className={`truncate text-[10px] sm:text-xs ${errorMsg ? 'text-red-500' : 'text-emerald-500'}`}> &gt; {errorMsg || statusMsg} </span> {isPlaying && !errorMsg && <Activity size={14} className="text-emerald-500 animate-pulse ml-2 flex-shrink-0" />} {isLoading && !errorMsg && <Zap size={14} className="text-amber-500 animate-pulse ml-2 flex-shrink-0" />} {isHandsFree && !isPlaying && !isLoading && !errorMsg && <Mic size={14} className="text-red-500 animate-pulse ml-2 flex-shrink-0" />} </div> </div> {/* Input Texto / Log */} <textarea value={text} onChange={(e) => setText(e.target.value)} className="w-full bg-neutral-950/50 border border-neutral-700 rounded p-2 text-xs text-neutral-300 focus:outline-none focus:border-emerald-500 resize-none h-20" placeholder={isHandsFree ? "Escuchando transcripción en tiempo real..." : "Escribe texto directo o activa Manos Libres..."} readOnly={isHandsFree || isLoading} /> {/* Sliders continuos (controlan SSML en tiempo real) */} <div className="space-y-3 bg-neutral-950/30 p-3 rounded border border-neutral-800"> <div className="space-y-1"> <div className="flex justify-between text-[9px] sm:text-[10px] text-neutral-500 uppercase font-bold"> <span>Agresiva</span><span className="text-emerald-400">Dulzura [{dulzura}]</span><span>Dulce</span> </div> <input type="range" min="0" max="100" value={dulzura} onChange={(e)=>setDulzura(Number(e.target.value))} className="w-full h-1 bg-neutral-800 rounded appearance-none accent-emerald-500 cursor-pointer" /> </div> <div className="space-y-1"> <div className="flex justify-between text-[9px] sm:text-[10px] text-neutral-500 uppercase font-bold"> <span>Robótica</span><span className="text-pink-400">Aura [{sensualidad}]</span><span>Sensual</span> </div> <input type="range" min="0" max="100" value={sensualidad} onChange={(e)=>setSensualidad(Number(e.target.value))} className="w-full h-1 bg-neutral-800 rounded appearance-none accent-pink-500 cursor-pointer" /> </div> <div className="space-y-1"> <div className="flex justify-between text-[9px] sm:text-[10px] text-neutral-500 uppercase font-bold"> <span>Atenuada</span><span className="text-amber-400">Intensidad [{intensidad}]</span><span>Fuerte</span> </div> <input type="range" min="0" max="100" value={intensidad} onChange={(e)=>setIntensidad(Number(e.target.value))} className="w-full h-1 bg-neutral-800 rounded appearance-none accent-amber-500 cursor-pointer" /> </div> </div> {/* Botones de Control */} <div className="flex flex-col sm:flex-row gap-2"> <button onClick={toggleHandsFree} disabled={isLoading} className={`flex-1 py-2 rounded text-xs font-bold flex items-center justify-center gap-2 transition-colors border ${ isHandsFree ? 'bg-red-900/20 text-red-400 border-red-900/50 hover:bg-red-900/40 shadow-[0_0_10px_rgba(239,68,68,0.2)]' : 'bg-indigo-900/20 text-indigo-400 border-indigo-900/50 hover:bg-indigo-900/40' }`} > {isHandsFree ? <MicOff size={14} /> : <Mic size={14} />} {isHandsFree ? 'Detener Escucha' : 'Manos Libres'} </button> <div className="flex gap-2 flex-1"> <button onClick={handleManualPlay} disabled={isLoading || isPlaying || isHandsFree} className="flex-1 bg-emerald-600/20 hover:bg-emerald-600/40 text-emerald-400 border border-emerald-600/50 disabled:opacity-30 py-2 rounded text-xs font-bold flex items-center justify-center gap-1 transition-colors" > {isLoading ? <Loader2 size={14} className="animate-spin" /> : <Play size={14} />} Sintetizar </button> <button onClick={stopAudio} disabled={!isPlaying && !isHandsFree} className="px-4 bg-neutral-800 hover:bg-neutral-700 text-neutral-400 border border-neutral-700 disabled:opacity-30 py-2 rounded text-xs font-bold flex items-center justify-center transition-colors" > <Square size={14} /> </button> </div> </div> {/* Botón para limpiar caché (opcional) */} <div className="text-right"> <button onClick={() => audioCache.clear()} className="text-[8px] text-neutral-600 hover:text-neutral-400 underline" > limpiar caché de audio </button> </div> </div> ); }; // --- ENTORNO ESCRITORIO (sin cambios) --- export default function App() { const [widgets, setWidgets] = useState({ voice: { isOpen: true, pos: { x: window.innerWidth > 768 ? window.innerWidth / 2 - 170 : 20, y: 40 } } }); const toggleWidget = (id) => { setWidgets(prev => ({ ...prev, [id]: { ...prev[id], isOpen: !prev[id].isOpen } })); }; return ( <div className="w-full h-screen bg-neutral-950 bg-[radial-gradient(ellipse_80%_80%_at_50%_-20%,rgba(16,185,129,0.1),rgba(0,0,0,1))] overflow-hidden relative font-sans text-neutral-200"> <div className="absolute inset-0 flex items-center justify-center opacity-[0.02] pointer-events-none"><Settings2 size={500} /></div> {widgets.voice.isOpen && ( <DraggableWidget title="MODULADOR VOCAL KORE" icon={Zap} initialPos={widgets.voice.pos} onClose={() => toggleWidget('voice')}> <VoiceModulatorWidget /> </DraggableWidget> )} <div className="absolute bottom-6 left-1/2 transform -translate-x-1/2 bg-neutral-900/80 backdrop-blur-md border border-neutral-700/50 p-2 rounded-2xl shadow-2xl flex gap-2 z-[100]"> <div className="px-3 flex items-center border-r border-neutral-700/50 text-neutral-500"><LayoutGrid size={20} /></div> <button onClick={() => toggleWidget('voice')} className={`px-4 py-2 rounded-xl flex items-center gap-2 text-sm font-medium transition-all ${

B&W Photo , Male A.I. inspired by SHODAN from System Shock, full body, detailed symmetrical face, real, alive, real skin textures, big eyes,, (B&W, Monochrome),Photorealistic, Hyper-realistic, Hyper-detailed, film noir, detailed skin, pores, matte skin, soft lighting, subsurface scattering, realistic, heavy shadow, masterpiece, best quality, 8k, golden ratio, Intricate, film photography, full sharp, soft focus,

“Młoda kobieta o owalnej twarzy i harmonijnych rysach. Ma mały, prosty, lekko zadarty nos oraz pełne, delikatnie szerokie usta. Jej brwi są cienkie, zadbane i lekko łukowate. Włosy blond, lekko falowane, sięgające ramion, zaczesane trochę na bok. Wysportowana sylwetka, proporcjonalna. Ubrana w jedwabną, zieloną piżamę, leży na swoim łóżku w zrelaksowanej pozycji. Patrzy w telefon, który trzyma w ręce, jednak jej dłoń nie jest widoczna w kadrze. Atmosfera obrazu jest przytulna i spokojna.”bauhaus furniture and decoration, high ceiling, beige blue salmon pastel palette, interior design magazine, cozy atmosphere; 8k, intricate detail, photorealistic, realistic light, wide angle, kinkfolk photography, A+D architecture

“Młoda kobieta o owalnej twarzy i harmonijnych rysach. Ma mały, prosty, lekko zadarty nos oraz pełne, delikatnie szerokie usta. Jej brwi są cienkie, zadbane i lekko łukowate. Włosy blond, lekko falowane, sięgające ramion, zaczesane trochę na bok. Wysportowana sylwetka, proporcjonalna. Ubrana w jedwabną, zieloną piżamę, leży na swoim łóżku w zrelaksowanej pozycji. Patrzy w telefon, który trzyma w ręce, jednak jej dłoń nie jest widoczna w kadrze. Atmosfera obrazu jest przytulna i spokojna.”bauhaus furniture and decoration, high ceiling, beige blue salmon pastel palette, interior design magazine, cozy atmosphere; 8k, intricate detail, photorealistic, realistic light, wide angle, kinkfolk photography, A+D architecture

ruda dziewczyna w gorsecie. Postać widziana w całości. Kobieta idzie na zakupy w zimowy dzień na manhattanie. Zdjęcie robione w ruchu. Hiperrealistyczna skóra i lawa, głębia ostrości. Zdjęcie robione aparatem canon miękkie światło. Aparat szerokokątny

请将下图中所有英文文字替换为对应的中文，图片的布局、结构、颜色、箭头、方框样式完全不变，仅替换文字内容。具体替换对应关系如下： - "True label" → "真实标签" - "Local data" → "本地数据" - "Pred" → "预测" - "Loss" → "损失" - "Trained with E local epochs" → "本地训练 E 个轮次" - "Upload local model parameters" → "上传本地模型参数" - "Client $\mathcal{C}_m$" → "客户端 $\mathcal{C}_m$" - "Local model parameters $W_m = W$" → "本地模型参数 $W_m = W$" - "$\mathcal{C}_m$ Download global model" → "$\mathcal{C}_m$ 下载全局模型" - "Initialize global model" → "初始化全局模型" - "Aggregate the global model" → "聚合全局模型" - "Server $\mathcal{S}$" → "服务端 $\mathcal{S}$" - "Global model parameters $W$" → "全局模型参数 $W$" - "Attacker download $\mathcal{C}_m$'s local model parameters" → "攻击者下载 $\mathcal{C}_m$ 的本地模型参数" - "Dummy label" → "虚假标签" - "Dummy data" → "虚假数据" - "Attacker" → "攻击者" - "Optimize" → "优化" - "Gradient matching" → "梯度匹配" - "Fig. 1. Gradients inversion attacks in federated learning." → "图1 联邦学习中的梯度反转攻击"

Black and White Portrait of a Young gothic lolita, Woman, grimdark style, Close-up, Pale Skins, heavy makeup, Depth of Fields, Bokeh, Analog Style, A photo by W. Eugene Smith, (B&W, Monochrome),Photorealistic, Hyper-realistic, Hyper-detailed, film noir, detailed skin, pores, matte skin, soft lighting, subsurface scattering, realistic, heavy shadow, masterpiece, best quality, 8k, golden ratio, Intricate, film photography, full sharp, soft focus,

Specialized Bitumen Refining Plant Governorate: Anbar / Hit District Production Capacity: ( ) Tons/Day The city of Hit in the Anbar Governorate is considered one of the most famous areas in the world for its natural "bitumen springs," which have been used for thousands of years (dating back to the Babylonian and Assyrian eras). However, processing this bitumen for modern use requires technical steps to transform it from a raw material into a viable product for construction or industrial applications. Bitumen emerges from these springs as a highly viscous liquid mixed with sulfurous water, salts, and mud impurities. This "Natural Asphalt" differs from petroleum bitumen produced in refineries, and it can also appear in the form of rocky or spongy blocks mixed with mud. To obtain industrially usable products from this bitumen, specifically for: 1. Waterproofing (Felt/Membranes): Considered one of the best coating materials for building foundations to prevent moisture leakage due to its high resistance to hydrolysis. 2. Road Paving: Mixed with gravel and sand to produce asphalt concrete. It is characterized by exceptionally high cohesive strength compared to industrial bitumen. The natural bitumen from these springs must undergo several fundamental processing stages to become industrially viable: 1. Collection and Sedimentation: Bitumen is collected from the springs or quarry sites and left in designated basins to allow the sulfurous water to naturally separate (due to density differences). 2. Primary Heating: The raw bitumen is placed in large boilers to: a. Evaporate the remaining water. b. Reduce viscosity for easier handling. 3. Filtration and Purification: The heated bitumen is screened to remove solid impurities such as gravel, dirt, and suspended organic matter. 4. Secondary Heating and Cooking: The temperature of the bitumen is raised, improving agents are added, and it is prepared for the vacuum distillation process. 5. Vacuum Distillation: The distillation process is conducted under low pressure (vacuum pressure), which allows for: a. The separation of light oils and volatile substances at lower temperatures. b. The production of highly pure "Hard Asphalt," which is highly demanded in the construction industry. ________________________________________ Plant Components and Operational Stages The specialized bitumen plant for processing raw natural bitumen (in both liquid and solid states) consists of a range of specialized equipment designed according to the latest international standards. This equipment aligns with the technical and engineering requirements for bitumen products, complies with Iraqi standard specifications, and adheres to environmental considerations in the Anbar Governorate. 1. Extraction Stage The raw material (solid or liquid) is extracted from quarries designated by the Geological Survey Authority using specialized mechanical equipment. It is stored in stocks or special basins for solid materials, then transported to the refinery site using specialized transport vehicles of various capacities. 2. Storage Stage The raw materials are stored in designated yards to ensure a sufficient inventory for continuous, uninterrupted production for no less than 7 working days. 3. Raw Material Preparation and Primary Heating Stage Raw materials are fed into the plant via hydraulic lifts. This stage includes: • 3-1: Crushing and Digestion: Solid raw materials from the quarries are broken down and digested using a digester (SH-01) equipped with double blades driven by hydraulic motors (22.5 kW capacity). The digester is 5 meters long and 1.80 meters in diameter, made of carbon steel, with Stainless Steel 304 blades. It includes a Stainless Steel piston driven by a 7.5 kW electric motor. • 3-2: Primary Heating: This melts the bitumen and improves pumpability through pipes and pumps. • 3-3: Efficiency Enhancement: To increase melting efficiency, Gas Oil is added to the primary heating basin at a ratio of 1:5 per ton of solid raw material entering the basin (this ratio decreases when using liquid raw bitumen). o 3-2-1: Primary Melting Basin (TK-01): Raw material is heated in a concrete tank (25m L x 5m W x 3m H) with a maximum storage capacity of 300 tons. Heating pipes circulate thermal fluid (oil) at 125°C, with a retention time of 4-6 hours. The tank is internally lined with 6-8 mm carbon steel plates to protect the heating pipes from corrosion. It contains 8 Stainless Steel 304 mixers (MX-01 A/B/C/D/E/F) driven by 7.5 kW electric motors (50 RPM) and gearboxes (1:60 ratio) to mix the material, increase heating efficiency, reduce retention time, and circulate the melted bitumen to eliminate dissolved water, resulting in a homogeneous melt. Covered with a carbon steel roof with service hatches, it connects to an air duct (30x60 cm) linked to 2 air blowers (AB-01A/B) (one operating, one standby) at 22.5 kW / 1500 RPM. These extract water vapor and sulfur fumes, sending them to a scrubber before atmospheric release and water recycling. o 3-2-2: Primary Collection Tank (V-01): A carbon steel tank (12-14 mm thick) with a maximum capacity of 125 tons (10m L x 5m W x 3m H). It connects directly to the primary tank (TK-01) via channels and movable gates to receive only liquid raw material. It contains thermal oil pipes to maintain the liquid raw material at 140°C. Insulated with glass wool (90 kg/m³) and a 1.8 mm aluminum outer cover. Impurities larger than 35 mm are removed and collected in a waste tank. o 3-2-3: Screw Conveyors (SC-01 A/B): Carbon steel screw conveyors with a double-jacketed outer cover filled with thermal oil to maintain the 140°C temperature. Driven by 22.5 kW electric motors (3000 RPM) with 1:40 gearboxes, they transport the liquid raw material to the preliminary filtration unit. 4. Purification Unit Removes suspended impurities from the liquid raw material in two stages: • 4-1: Preliminary Purification Tank (V-02): A carbon steel tank (12-14 mm thick, 125-ton capacity, 5m L x 10m W x 3m H). Receives liquid raw material from the primary collection tank. Contains thermal oil pipes to maintain 140°C. Insulated with glass wool (90 kg/m³) and a 1.8 mm aluminum cover. Impurities larger than 15 mm are removed to a waste tank. Material is pumped to the final filtration stage via gear pumps (GP-01 A/B) (one operating, one standby) at 22.5 kW / 1000 RPM. • 4-2: Final Filtration Unit (FT-01): Removes remaining impurities by passing liquids through box filters arranged in 2 trains (8 per train). They feature a two-layer Stainless Steel filter mesh (specified microns) wrapped around square boxes. Liquid enters from the outside, and pure liquid is collected from the inside via a pipe network connected to a manifold. This is driven by two vacuum pumps (VP-01A/B) connected to the raw material tanks. 5. Raw Material Tanks (V-03 A-J) Ten carbon steel tanks (2.5m diameter, 9m length, 14 mm thickness, 45-ton max capacity) equipped with thermal oil heating coils. They receive, store, and prepare the purified raw material for the subsequent cooking reaction. Insulated with glass wool (90 kg/m³) and a 1.8 mm aluminum cover. Connected by a pipe/valve network, the material is pumped via two centrifugal pumps (P-01 A/B) at 22.5 kW / 3000 RPM to the reactor unit. The tanks connect to a pipe network driven by vacuum pumps (VP-01A/B) at 22.5 kW / 1500 RPM, pushing heating gases and vapors to the gas washing tank (V-14). 6. Reactor (Cooking) Unit (V-04 A/B) Consists of three reactors (55 tons each) that prepare the raw material for vacuum distillation and extract light naphtha compounds. • 6-1: Cooking Process: o 6-1-1: Catalyst System: Consists of two tanks. One prepares the catalyst mixture (1.5m dia, 4m H, 8mm carbon steel) with a mixer (MX-03) driven by a hydromotor and 1:40 gearbox. The second stores Gas Oil added to the preparation unit (1.5m dia, 1m H, 5mm carbon steel) with a 0.5 HP centrifugal pump. o 6-1-2: Reaction Tanks (V-04/05/06A): Three carbon steel tanks (2.8m dia, 9m L, 14mm thick, 55-ton max). Each has 2 Stainless Steel mixers (MX-02 A/B/C/D/E/F) driven by a 7.5 kW motor (1500 RPM) with a 1:40 gearbox. Contains an internal heating system powered by a Gas Oil burner to raise the temperature to 180°C. Catalyst is injected via dosing pumps (DP-01A/B) to increase naphtha extraction efficiency. Material is circulated during cooking by two centrifugal pumps per reactor (P-04A/B/C/D/E/F) (one active, one standby) to reduce retention time to 3-4 hours. After cooking, material is moved to the attached tank (V-04/05/06B) for storage before distillation. Fully insulated. o 6-1-3: Cooked Material Tank (V-04/05/06B): Carbon steel tank (2.8m dia, 9m L, 14mm thick) with thermal oil pipes to maintain 190-200°C. Fully insulated. Material is pumped to the vacuum distillation tower via centrifugal pumps (P-05A/B) (one active, one standby) at 22.5 kW / 3000 RPM. 7. Raw Naphtha Storage Unit Collects and condenses naphtha extracted during cooking. • 7-1-1: Raw Naphtha Tanks (V-07A/B/C): Three vertical Stainless Steel 304 tanks (1.5m dia, 5m H) connected to three heat exchangers and two pump pairs. Equipped internally with water spray nozzles on a ring pipe to wash non-condensable gases. • 7-1-2: Heat Exchangers (HE-01A/B/C): Condense naphtha vapors from 140°C down to 40°C using water from the cooling tower. Connected in series. Shell & Tube type, carbon steel (510 mm dia, 6m L) with 70 tubes (0.75-inch dia) in two rows of 35. Includes internal baffles for efficiency. • 7-1-3: Supporting Pumps: Vacuum pumps (VP-01A/B) at 22.5 kW / 1500 RPM draw naphtha vapors from reactors to the heat exchangers, pushing non-condensable gases to the scrubber (V-14). Centrifugal pumps (P-02A/B) at 11.5 kW / 1500 RPM transport liquid raw naphtha to the Bleaching Unit. 8. Vacuum Distillation Unit The core of the plant, separating remaining light compounds and producing hard asphalt. • 8-1-1: Vacuum Distillation Tower: A vertical tower (~16m total height, 14mm carbon steel). Bottom section (Reboiler) is 3.5m dia x 1.2m H; top section is 1.5m dia x 12m H. Fully insulated. Fed with cooked material at 190-200°C via pumps (P-05A/B). To start extraction (remaining naphtha, Gas Oil, diesel), temperature is raised to 240-250°C using Heating Coil 1 via pumps (P-08A/B) at 55 kW / 3000 RPM, with continuous circulation via pumps (P-07A/B). Vacuum pumps (VP-03A/B) maintain 0.3-0.5 mbar pressure. Light compounds are extracted, condensed (HE-02A/B/C), and stored (V-08/09/10 A/B) over 2.5-3 hours. Afterward, material is heated via Heating Coil 2 to 320-340°C to finalize extraction and produce hard bitumen. Product is extracted via pumps (P-07A/B) at ~320°C, cooled via cooling tower coils, and sent to final tanks (V-18A/B/C). Batch processing takes 6-7 hours daily; continuous operation is possible. • 8-1-2: Supporting Pumps: Vacuum pumps (VP-03A/B) at 5.5 kW / 3000 RPM draw light vapors for condensation. Circulation centrifugal pumps (P-08A/B) at 55 kW move hot material to heating coils; (P-07A/B) circulate material and pump final bitumen product. • 8-1-3: Heating Coils 1 & 2: Carbon steel 4-inch diameter coils heated externally by a Gas Oil burner. Connected in series to heat liquid bitumen in two stages to prevent degradation. • 8-2: Heat Exchangers (HE-02A/B/C): Condense light compound vapors from 240°C to 40°C. Shell & Tube type, carbon steel (600 mm dia, 6m L) with 80 tubes (1-inch dia) in two rows of 40, equipped with baffles. • 8-3: Light Compound Tanks (V-08A/B, V-09A/B, V-10A/B): Six horizontal carbon steel tanks (1.5m dia, 4.5m L, 14mm thick). Receive condensates, linked to heat exchangers and vacuum pumps. Liquids are pumped to the Bleaching Unit via centrifugal pumps (P-06A/B) at 7.5 kW / 1500 RPM. 9. Bleaching Unit Improves the specifications of raw light compounds for local use and marketing. • 9-1: Collection Tank (V-11): Horizontal carbon steel tank (1m dia, 2.5m L, 14mm thick) placed above the system to store and distribute light compounds to the bleaching columns. • 9-2: Bleaching Columns (V-12A/B/C): Three vertical carbon steel vessels (1m dia, 4.5m H, 14mm thick). Contain a 15 cm catalyst layer on trays to bleach raw liquids into high-quality compounds, collected in a bottom horizontal tank. The catalyst is a calcined mixture of Bentonite and Zinc Oxide granules (2-3 mm) homogenized in water, which can be reactivated with steam and 5% HCl. • 9-3: Supporting Pumps: Vacuum pumps (VP-04A/B) at 5.5 kW extract vapors to the scrubber. Centrifugal pumps (P-09A/B) at 7.5 kW push bleached liquids to final tanks. 10. Production Tanks (V-13 A-F & V-18 A-C) • Light Products: Six horizontal carbon steel tanks (2.8m dia, 9m L, 55-ton capacity). V-13A/B for light naphtha, V-13C/D for Gas Oil, V-13E/F for diesel. • Asphalt: Three vertical carbon steel tanks (V-18A/B/C) (5m dia, 9m H). Equipped with thermal oil heating coils to keep asphalt liquid. Fully insulated (90 kg/m³ glass wool, 1.8mm aluminum cover). 11. Supporting Systems • 11-1: Gas Washing (Scrubber) System: Treats non-condensable gases before atmospheric release. Contains V-14 washing tank (1m dia, 2.8m L), a 500mm Flare stack with 3 ignitors, and a 1m x 1m LPG tank (V-15) for ignition. • 11-2: Cooling Tower: Provides cooling water for heat exchangers. Galvanized pressed steel basin (16m L x 2.4m W x 2.8m H), FRP casing, top fans, water distributors, and fill media. Includes Accumulator tank V-20 (1.5m dia, 2m L) and 11 kW pushing pumps (P-14A/B). • 11-3: Thermal Oil Boilers: Includes oil tank, heating boiler, oil pumps, and heating accelerators. • 11-4: Distillation Tower Raw Boilers • 11-5: Power Generation System • 11-6: Production Laboratory • 11-7: Control and Operation Room • 11-8: Catalyst System: Contains a vertical diesel tank (1m dia, 1.5m H) with a 1 kW centrifugal pump (P-11). Two vertical carbon steel tanks (V-17A/B, 1.5m dia, 4.5m H) with an MX-03 hydromotor mixer (7.5 kW, 30 RPM). V-17A is for preparation, V-17B pumps catalyst to the reactor. ________________________________________ Catalyst Chemical Components & Formulations 1. Alumina (Al2O3): Enhances the cracking of chemical bonds in heavy bitumen chains and increases Gas Oil extraction yield. 2. Manganese Dioxide (MnO2): Accelerates the reaction, reduces reaction time, and acts as a gasoline improver. 3. Silicon Dioxide (SiO2): Increases acceleration and reduces reaction time. 4. Iron Oxides (Fe2O): Accelerates the reaction, prevents pipe corrosion, and stops sulfur and wax from sticking to pipes and pumps. Weight Ratios (WT/WT) to Produce One Barrel (200 Liters) of Catalyst: 1. Alumina: Varies by feed: 2-2.5% for Bitumen / 4-5% for Vacuum Residue (VR) / 2-2.5% for Heavy Fuel Oil (HFO). To increase Gas Oil/Diesel (Light fuel) yield, Alumina can be added up to a maximum of 10%. 2. Manganese Dioxide: 2-2.5% for HFO / 4-5% for VR and Bitumen. 3. Iron Oxides: 2-2.5% across all feeds. 4. Silicon Dioxide: 2-2.5% for HFO / 4-5% for Bitumen and VR. 5. Remaining Volume: Filled with C-oil. Note: One barrel (200 Liters) of this mixture is added for every 5 tons of HFO, VR, or Bitumen. Manufacturing Mechanism: All components are placed in a tank, initially mixed with water, and heated to 80-120°C with continuous mixing (20-30 RPM). Once foam is generated, the product is allowed to cool to 80°C. The heating process up to 120°C is repeated 3 or 4 times until foaming ceases. Finally, the temperature is raised to 150°C, and the mixture is topped off to 200 liters using C-oil. To further improve light compound specifications, Zinc Oxide (300 grams) is mixed with 20 kg of Bentonite in C-oil. This is added alongside the catalyst at a ratio of 1/5 barrel of catalyst added to the reactor.

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Specialized Bitumen Refining Plant Governorate: Anbar / Hit District Production Capacity: ( ) Tons/Day The city of Hit in the Anbar Governorate is considered one of the most famous areas in the world for its natural "bitumen springs," which have been used for thousands of years (dating back to the Babylonian and Assyrian eras). However, processing this bitumen for modern use requires technical steps to transform it from a raw material into a viable product for construction or industrial applications. Bitumen emerges from these springs as a highly viscous liquid mixed with sulfurous water, salts, and mud impurities. This "Natural Asphalt" differs from petroleum bitumen produced in refineries, and it can also appear in the form of rocky or spongy blocks mixed with mud. To obtain industrially usable products from this bitumen, specifically for: 1. Waterproofing (Felt/Membranes): Considered one of the best coating materials for building foundations to prevent moisture leakage due to its high resistance to hydrolysis. 2. Road Paving: Mixed with gravel and sand to produce asphalt concrete. It is characterized by exceptionally high cohesive strength compared to industrial bitumen. The natural bitumen from these springs must undergo several fundamental processing stages to become industrially viable: 1. Collection and Sedimentation: Bitumen is collected from the springs or quarry sites and left in designated basins to allow the sulfurous water to naturally separate (due to density differences). 2. Primary Heating: The raw bitumen is placed in large boilers to: a. Evaporate the remaining water. b. Reduce viscosity for easier handling. 3. Filtration and Purification: The heated bitumen is screened to remove solid impurities such as gravel, dirt, and suspended organic matter. 4. Secondary Heating and Cooking: The temperature of the bitumen is raised, improving agents are added, and it is prepared for the vacuum distillation process. 5. Vacuum Distillation: The distillation process is conducted under low pressure (vacuum pressure), which allows for: a. The separation of light oils and volatile substances at lower temperatures. b. The production of highly pure "Hard Asphalt," which is highly demanded in the construction industry. ________________________________________ Plant Components and Operational Stages The specialized bitumen plant for processing raw natural bitumen (in both liquid and solid states) consists of a range of specialized equipment designed according to the latest international standards. This equipment aligns with the technical and engineering requirements for bitumen products, complies with Iraqi standard specifications, and adheres to environmental considerations in the Anbar Governorate. 1. Extraction Stage The raw material (solid or liquid) is extracted from quarries designated by the Geological Survey Authority using specialized mechanical equipment. It is stored in stocks or special basins for solid materials, then transported to the refinery site using specialized transport vehicles of various capacities. 2. Storage Stage The raw materials are stored in designated yards to ensure a sufficient inventory for continuous, uninterrupted production for no less than 7 working days. 3. Raw Material Preparation and Primary Heating Stage Raw materials are fed into the plant via hydraulic lifts. This stage includes: • 3-1: Crushing and Digestion: Solid raw materials from the quarries are broken down and digested using a digester (SH-01) equipped with double blades driven by hydraulic motors (22.5 kW capacity). The digester is 5 meters long and 1.80 meters in diameter, made of carbon steel, with Stainless Steel 304 blades. It includes a Stainless Steel piston driven by a 7.5 kW electric motor. • 3-2: Primary Heating: This melts the bitumen and improves pumpability through pipes and pumps. • 3-3: Efficiency Enhancement: To increase melting efficiency, Gas Oil is added to the primary heating basin at a ratio of 1:5 per ton of solid raw material entering the basin (this ratio decreases when using liquid raw bitumen). o 3-2-1: Primary Melting Basin (TK-01): Raw material is heated in a concrete tank (25m L x 5m W x 3m H) with a maximum storage capacity of 300 tons. Heating pipes circulate thermal fluid (oil) at 125°C, with a retention time of 4-6 hours. The tank is internally lined with 6-8 mm carbon steel plates to protect the heating pipes from corrosion. It contains 8 Stainless Steel 304 mixers (MX-01 A/B/C/D/E/F) driven by 7.5 kW electric motors (50 RPM) and gearboxes (1:60 ratio) to mix the material, increase heating efficiency, reduce retention time, and circulate the melted bitumen to eliminate dissolved water, resulting in a homogeneous melt. Covered with a carbon steel roof with service hatches, it connects to an air duct (30x60 cm) linked to 2 air blowers (AB-01A/B) (one operating, one standby) at 22.5 kW / 1500 RPM. These extract water vapor and sulfur fumes, sending them to a scrubber before atmospheric release and water recycling. o 3-2-2: Primary Collection Tank (V-01): A carbon steel tank (12-14 mm thick) with a maximum capacity of 125 tons (10m L x 5m W x 3m H). It connects directly to the primary tank (TK-01) via channels and movable gates to receive only liquid raw material. It contains thermal oil pipes to maintain the liquid raw material at 140°C. Insulated with glass wool (90 kg/m³) and a 1.8 mm aluminum outer cover. Impurities larger than 35 mm are removed and collected in a waste tank. o 3-2-3: Screw Conveyors (SC-01 A/B): Carbon steel screw conveyors with a double-jacketed outer cover filled with thermal oil to maintain the 140°C temperature. Driven by 22.5 kW electric motors (3000 RPM) with 1:40 gearboxes, they transport the liquid raw material to the preliminary filtration unit. 4. Purification Unit Removes suspended impurities from the liquid raw material in two stages: • 4-1: Preliminary Purification Tank (V-02): A carbon steel tank (12-14 mm thick, 125-ton capacity, 5m L x 10m W x 3m H). Receives liquid raw material from the primary collection tank. Contains thermal oil pipes to maintain 140°C. Insulated with glass wool (90 kg/m³) and a 1.8 mm aluminum cover. Impurities larger than 15 mm are removed to a waste tank. Material is pumped to the final filtration stage via gear pumps (GP-01 A/B) (one operating, one standby) at 22.5 kW / 1000 RPM. • 4-2: Final Filtration Unit (FT-01): Removes remaining impurities by passing liquids through box filters arranged in 2 trains (8 per train). They feature a two-layer Stainless Steel filter mesh (specified microns) wrapped around square boxes. Liquid enters from the outside, and pure liquid is collected from the inside via a pipe network connected to a manifold. This is driven by two vacuum pumps (VP-01A/B) connected to the raw material tanks. 5. Raw Material Tanks (V-03 A-J) Ten carbon steel tanks (2.5m diameter, 9m length, 14 mm thickness, 45-ton max capacity) equipped with thermal oil heating coils. They receive, store, and prepare the purified raw material for the subsequent cooking reaction. Insulated with glass wool (90 kg/m³) and a 1.8 mm aluminum cover. Connected by a pipe/valve network, the material is pumped via two centrifugal pumps (P-01 A/B) at 22.5 kW / 3000 RPM to the reactor unit. The tanks connect to a pipe network driven by vacuum pumps (VP-01A/B) at 22.5 kW / 1500 RPM, pushing heating gases and vapors to the gas washing tank (V-14). 6. Reactor (Cooking) Unit (V-04 A/B) Consists of three reactors (55 tons each) that prepare the raw material for vacuum distillation and extract light naphtha compounds. • 6-1: Cooking Process: o 6-1-1: Catalyst System: Consists of two tanks. One prepares the catalyst mixture (1.5m dia, 4m H, 8mm carbon steel) with a mixer (MX-03) driven by a hydromotor and 1:40 gearbox. The second stores Gas Oil added to the preparation unit (1.5m dia, 1m H, 5mm carbon steel) with a 0.5 HP centrifugal pump. o 6-1-2: Reaction Tanks (V-04/05/06A): Three carbon steel tanks (2.8m dia, 9m L, 14mm thick, 55-ton max). Each has 2 Stainless Steel mixers (MX-02 A/B/C/D/E/F) driven by a 7.5 kW motor (1500 RPM) with a 1:40 gearbox. Contains an internal heating system powered by a Gas Oil burner to raise the temperature to 180°C. Catalyst is injected via dosing pumps (DP-01A/B) to increase naphtha extraction efficiency. Material is circulated during cooking by two centrifugal pumps per reactor (P-04A/B/C/D/E/F) (one active, one standby) to reduce retention time to 3-4 hours. After cooking, material is moved to the attached tank (V-04/05/06B) for storage before distillation. Fully insulated. o 6-1-3: Cooked Material Tank (V-04/05/06B): Carbon steel tank (2.8m dia, 9m L, 14mm thick) with thermal oil pipes to maintain 190-200°C. Fully insulated. Material is pumped to the vacuum distillation tower via centrifugal pumps (P-05A/B) (one active, one standby) at 22.5 kW / 3000 RPM. 7. Raw Naphtha Storage Unit Collects and condenses naphtha extracted during cooking. • 7-1-1: Raw Naphtha Tanks (V-07A/B/C): Three vertical Stainless Steel 304 tanks (1.5m dia, 5m H) connected to three heat exchangers and two pump pairs. Equipped internally with water spray nozzles on a ring pipe to wash non-condensable gases. • 7-1-2: Heat Exchangers (HE-01A/B/C): Condense naphtha vapors from 140°C down to 40°C using water from the cooling tower. Connected in series. Shell & Tube type, carbon steel (510 mm dia, 6m L) with 70 tubes (0.75-inch dia) in two rows of 35. Includes internal baffles for efficiency. • 7-1-3: Supporting Pumps: Vacuum pumps (VP-01A/B) at 22.5 kW / 1500 RPM draw naphtha vapors from reactors to the heat exchangers, pushing non-condensable gases to the scrubber (V-14). Centrifugal pumps (P-02A/B) at 11.5 kW / 1500 RPM transport liquid raw naphtha to the Bleaching Unit. 8. Vacuum Distillation Unit The core of the plant, separating remaining light compounds and producing hard asphalt. • 8-1-1: Vacuum Distillation Tower: A vertical tower (~16m total height, 14mm carbon steel). Bottom section (Reboiler) is 3.5m dia x 1.2m H; top section is 1.5m dia x 12m H. Fully insulated. Fed with cooked material at 190-200°C via pumps (P-05A/B). To start extraction (remaining naphtha, Gas Oil, diesel), temperature is raised to 240-250°C using Heating Coil 1 via pumps (P-08A/B) at 55 kW / 3000 RPM, with continuous circulation via pumps (P-07A/B). Vacuum pumps (VP-03A/B) maintain 0.3-0.5 mbar pressure. Light compounds are extracted, condensed (HE-02A/B/C), and stored (V-08/09/10 A/B) over 2.5-3 hours. Afterward, material is heated via Heating Coil 2 to 320-340°C to finalize extraction and produce hard bitumen. Product is extracted via pumps (P-07A/B) at ~320°C, cooled via cooling tower coils, and sent to final tanks (V-18A/B/C). Batch processing takes 6-7 hours daily; continuous operation is possible. • 8-1-2: Supporting Pumps: Vacuum pumps (VP-03A/B) at 5.5 kW / 3000 RPM draw light vapors for condensation. Circulation centrifugal pumps (P-08A/B) at 55 kW move hot material to heating coils; (P-07A/B) circulate material and pump final bitumen product. • 8-1-3: Heating Coils 1 & 2: Carbon steel 4-inch diameter coils heated externally by a Gas Oil burner. Connected in series to heat liquid bitumen in two stages to prevent degradation. • 8-2: Heat Exchangers (HE-02A/B/C): Condense light compound vapors from 240°C to 40°C. Shell & Tube type, carbon steel (600 mm dia, 6m L) with 80 tubes (1-inch dia) in two rows of 40, equipped with baffles. • 8-3: Light Compound Tanks (V-08A/B, V-09A/B, V-10A/B): Six horizontal carbon steel tanks (1.5m dia, 4.5m L, 14mm thick). Receive condensates, linked to heat exchangers and vacuum pumps. Liquids are pumped to the Bleaching Unit via centrifugal pumps (P-06A/B) at 7.5 kW / 1500 RPM. 9. Bleaching Unit Improves the specifications of raw light compounds for local use and marketing. • 9-1: Collection Tank (V-11): Horizontal carbon steel tank (1m dia, 2.5m L, 14mm thick) placed above the system to store and distribute light compounds to the bleaching columns. • 9-2: Bleaching Columns (V-12A/B/C): Three vertical carbon steel vessels (1m dia, 4.5m H, 14mm thick). Contain a 15 cm catalyst layer on trays to bleach raw liquids into high-quality compounds, collected in a bottom horizontal tank. The catalyst is a calcined mixture of Bentonite and Zinc Oxide granules (2-3 mm) homogenized in water, which can be reactivated with steam and 5% HCl. • 9-3: Supporting Pumps: Vacuum pumps (VP-04A/B) at 5.5 kW extract vapors to the scrubber. Centrifugal pumps (P-09A/B) at 7.5 kW push bleached liquids to final tanks. 10. Production Tanks (V-13 A-F & V-18 A-C) • Light Products: Six horizontal carbon steel tanks (2.8m dia, 9m L, 55-ton capacity). V-13A/B for light naphtha, V-13C/D for Gas Oil, V-13E/F for diesel. • Asphalt: Three vertical carbon steel tanks (V-18A/B/C) (5m dia, 9m H). Equipped with thermal oil heating coils to keep asphalt liquid. Fully insulated (90 kg/m³ glass wool, 1.8mm aluminum cover). 11. Supporting Systems • 11-1: Gas Washing (Scrubber) System: Treats non-condensable gases before atmospheric release. Contains V-14 washing tank (1m dia, 2.8m L), a 500mm Flare stack with 3 ignitors, and a 1m x 1m LPG tank (V-15) for ignition. • 11-2: Cooling Tower: Provides cooling water for heat exchangers. Galvanized pressed steel basin (16m L x 2.4m W x 2.8m H), FRP casing, top fans, water distributors, and fill media. Includes Accumulator tank V-20 (1.5m dia, 2m L) and 11 kW pushing pumps (P-14A/B). • 11-3: Thermal Oil Boilers: Includes oil tank, heating boiler, oil pumps, and heating accelerators. • 11-4: Distillation Tower Raw Boilers • 11-5: Power Generation System • 11-6: Production Laboratory • 11-7: Control and Operation Room • 11-8: Catalyst System: Contains a vertical diesel tank (1m dia, 1.5m H) with a 1 kW centrifugal pump (P-11). Two vertical carbon steel tanks (V-17A/B, 1.5m dia, 4.5m H) with an MX-03 hydromotor mixer (7.5 kW, 30 RPM). V-17A is for preparation, V-17B pumps catalyst to the reactor. ________________________________________ Catalyst Chemical Components & Formulations 1. Alumina (Al2O3): Enhances the cracking of chemical bonds in heavy bitumen chains and increases Gas Oil extraction yield. 2. Manganese Dioxide (MnO2): Accelerates the reaction, reduces reaction time, and acts as a gasoline improver. 3. Silicon Dioxide (SiO2): Increases acceleration and reduces reaction time. 4. Iron Oxides (Fe2O): Accelerates the reaction, prevents pipe corrosion, and stops sulfur and wax from sticking to pipes and pumps. Weight Ratios (WT/WT) to Produce One Barrel (200 Liters) of Catalyst: 1. Alumina: Varies by feed: 2-2.5% for Bitumen / 4-5% for Vacuum Residue (VR) / 2-2.5% for Heavy Fuel Oil (HFO). To increase Gas Oil/Diesel (Light fuel) yield, Alumina can be added up to a maximum of 10%. 2. Manganese Dioxide: 2-2.5% for HFO / 4-5% for VR and Bitumen. 3. Iron Oxides: 2-2.5% across all feeds. 4. Silicon Dioxide: 2-2.5% for HFO / 4-5% for Bitumen and VR. 5. Remaining Volume: Filled with C-oil. Note: One barrel (200 Liters) of this mixture is added for every 5 tons of HFO, VR, or Bitumen. Manufacturing Mechanism: All components are placed in a tank, initially mixed with water, and heated to 80-120°C with continuous mixing (20-30 RPM). Once foam is generated, the product is allowed to cool to 80°C. The heating process up to 120°C is repeated 3 or 4 times until foaming ceases. Finally, the temperature is raised to 150°C, and the mixture is topped off to 200 liters using C-oil. To further improve light compound specifications, Zinc Oxide (300 grams) is mixed with 20 kg of Bentonite in C-oil. This is added alongside the catalyst at a ratio of 1/5 barrel of catalyst added to the reactor.

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Wyobraź sobie... ...świat pokryty grubą, puchatą kołderką śniegu. Każdy krok skrzypi miękko, jakbyś szedł po dywanie z waty. Drzewa stoją nieruchomo, obwieszone lśniącymi szronami, które mienią się w promieniach słońca. Powietrze jest tak czyste i chruści, że aż ściska za serce. Niebo jest bezkresne, błękitne, a słońce świeci jasno, choć nie przygrzewa. Jego promienie odbijają się od śniegu, tworząc olśniewającą poświatę. Cienie drzew są długie i ostre, podkreślające zimową scenerię. Mróz szczypie w policzki, a oddech zamienia się w małe chmurki pary. Jednak to właśnie ten chłód sprawia, że czujemy się żywi i pełni energii.

Specialized Bitumen Refining Plant Governorate: Anbar / Hit District Production Capacity: ( ) Tons/Day The city of Hit in the Anbar Governorate is considered one of the most famous areas in the world for its natural "bitumen springs," which have been used for thousands of years (dating back to the Babylonian and Assyrian eras). However, processing this bitumen for modern use requires technical steps to transform it from a raw material into a viable product for construction or industrial applications. Bitumen emerges from these springs as a highly viscous liquid mixed with sulfurous water, salts, and mud impurities. This "Natural Asphalt" differs from petroleum bitumen produced in refineries, and it can also appear in the form of rocky or spongy blocks mixed with mud. To obtain industrially usable products from this bitumen, specifically for: 1. Waterproofing (Felt/Membranes): Considered one of the best coating materials for building foundations to prevent moisture leakage due to its high resistance to hydrolysis. 2. Road Paving: Mixed with gravel and sand to produce asphalt concrete. It is characterized by exceptionally high cohesive strength compared to industrial bitumen. The natural bitumen from these springs must undergo several fundamental processing stages to become industrially viable: 1. Collection and Sedimentation: Bitumen is collected from the springs or quarry sites and left in designated basins to allow the sulfurous water to naturally separate (due to density differences). 2. Primary Heating: The raw bitumen is placed in large boilers to: a. Evaporate the remaining water. b. Reduce viscosity for easier handling. 3. Filtration and Purification: The heated bitumen is screened to remove solid impurities such as gravel, dirt, and suspended organic matter. 4. Secondary Heating and Cooking: The temperature of the bitumen is raised, improving agents are added, and it is prepared for the vacuum distillation process. 5. Vacuum Distillation: The distillation process is conducted under low pressure (vacuum pressure), which allows for: a. The separation of light oils and volatile substances at lower temperatures. b. The production of highly pure "Hard Asphalt," which is highly demanded in the construction industry. ________________________________________ Plant Components and Operational Stages The specialized bitumen plant for processing raw natural bitumen (in both liquid and solid states) consists of a range of specialized equipment designed according to the latest international standards. This equipment aligns with the technical and engineering requirements for bitumen products, complies with Iraqi standard specifications, and adheres to environmental considerations in the Anbar Governorate. 1. Extraction Stage The raw material (solid or liquid) is extracted from quarries designated by the Geological Survey Authority using specialized mechanical equipment. It is stored in stocks or special basins for solid materials, then transported to the refinery site using specialized transport vehicles of various capacities. 2. Storage Stage The raw materials are stored in designated yards to ensure a sufficient inventory for continuous, uninterrupted production for no less than 7 working days. 3. Raw Material Preparation and Primary Heating Stage Raw materials are fed into the plant via hydraulic lifts. This stage includes: • 3-1: Crushing and Digestion: Solid raw materials from the quarries are broken down and digested using a digester (SH-01) equipped with double blades driven by hydraulic motors (22.5 kW capacity). The digester is 5 meters long and 1.80 meters in diameter, made of carbon steel, with Stainless Steel 304 blades. It includes a Stainless Steel piston driven by a 7.5 kW electric motor. • 3-2: Primary Heating: This melts the bitumen and improves pumpability through pipes and pumps. • 3-3: Efficiency Enhancement: To increase melting efficiency, Gas Oil is added to the primary heating basin at a ratio of 1:5 per ton of solid raw material entering the basin (this ratio decreases when using liquid raw bitumen). o 3-2-1: Primary Melting Basin (TK-01): Raw material is heated in a concrete tank (25m L x 5m W x 3m H) with a maximum storage capacity of 300 tons. Heating pipes circulate thermal fluid (oil) at 125°C, with a retention time of 4-6 hours. The tank is internally lined with 6-8 mm carbon steel plates to protect the heating pipes from corrosion. It contains 8 Stainless Steel 304 mixers (MX-01 A/B/C/D/E/F) driven by 7.5 kW electric motors (50 RPM) and gearboxes (1:60 ratio) to mix the material, increase heating efficiency, reduce retention time, and circulate the melted bitumen to eliminate dissolved water, resulting in a homogeneous melt. Covered with a carbon steel roof with service hatches, it connects to an air duct (30x60 cm) linked to 2 air blowers (AB-01A/B) (one operating, one standby) at 22.5 kW / 1500 RPM. These extract water vapor and sulfur fumes, sending them to a scrubber before atmospheric release and water recycling. o 3-2-2: Primary Collection Tank (V-01): A carbon steel tank (12-14 mm thick) with a maximum capacity of 125 tons (10m L x 5m W x 3m H). It connects directly to the primary tank (TK-01) via channels and movable gates to receive only liquid raw material. It contains thermal oil pipes to maintain the liquid raw material at 140°C. Insulated with glass wool (90 kg/m³) and a 1.8 mm aluminum outer cover. Impurities larger than 35 mm are removed and collected in a waste tank. o 3-2-3: Screw Conveyors (SC-01 A/B): Carbon steel screw conveyors with a double-jacketed outer cover filled with thermal oil to maintain the 140°C temperature. Driven by 22.5 kW electric motors (3000 RPM) with 1:40 gearboxes, they transport the liquid raw material to the preliminary filtration unit. 4. Purification Unit Removes suspended impurities from the liquid raw material in two stages: • 4-1: Preliminary Purification Tank (V-02): A carbon steel tank (12-14 mm thick, 125-ton capacity, 5m L x 10m W x 3m H). Receives liquid raw material from the primary collection tank. Contains thermal oil pipes to maintain 140°C. Insulated with glass wool (90 kg/m³) and a 1.8 mm aluminum cover. Impurities larger than 15 mm are removed to a waste tank. Material is pumped to the final filtration stage via gear pumps (GP-01 A/B) (one operating, one standby) at 22.5 kW / 1000 RPM. • 4-2: Final Filtration Unit (FT-01): Removes remaining impurities by passing liquids through box filters arranged in 2 trains (8 per train). They feature a two-layer Stainless Steel filter mesh (specified microns) wrapped around square boxes. Liquid enters from the outside, and pure liquid is collected from the inside via a pipe network connected to a manifold. This is driven by two vacuum pumps (VP-01A/B) connected to the raw material tanks. 5. Raw Material Tanks (V-03 A-J) Ten carbon steel tanks (2.5m diameter, 9m length, 14 mm thickness, 45-ton max capacity) equipped with thermal oil heating coils. They receive, store, and prepare the purified raw material for the subsequent cooking reaction. Insulated with glass wool (90 kg/m³) and a 1.8 mm aluminum cover. Connected by a pipe/valve network, the material is pumped via two centrifugal pumps (P-01 A/B) at 22.5 kW / 3000 RPM to the reactor unit. The tanks connect to a pipe network driven by vacuum pumps (VP-01A/B) at 22.5 kW / 1500 RPM, pushing heating gases and vapors to the gas washing tank (V-14). 6. Reactor (Cooking) Unit (V-04 A/B) Consists of three reactors (55 tons each) that prepare the raw material for vacuum distillation and extract light naphtha compounds. • 6-1: Cooking Process: o 6-1-1: Catalyst System: Consists of two tanks. One prepares the catalyst mixture (1.5m dia, 4m H, 8mm carbon steel) with a mixer (MX-03) driven by a hydromotor and 1:40 gearbox. The second stores Gas Oil added to the preparation unit (1.5m dia, 1m H, 5mm carbon steel) with a 0.5 HP centrifugal pump. o 6-1-2: Reaction Tanks (V-04/05/06A): Three carbon steel tanks (2.8m dia, 9m L, 14mm thick, 55-ton max). Each has 2 Stainless Steel mixers (MX-02 A/B/C/D/E/F) driven by a 7.5 kW motor (1500 RPM) with a 1:40 gearbox. Contains an internal heating system powered by a Gas Oil burner to raise the temperature to 180°C. Catalyst is injected via dosing pumps (DP-01A/B) to increase naphtha extraction efficiency. Material is circulated during cooking by two centrifugal pumps per reactor (P-04A/B/C/D/E/F) (one active, one standby) to reduce retention time to 3-4 hours. After cooking, material is moved to the attached tank (V-04/05/06B) for storage before distillation. Fully insulated. o 6-1-3: Cooked Material Tank (V-04/05/06B): Carbon steel tank (2.8m dia, 9m L, 14mm thick) with thermal oil pipes to maintain 190-200°C. Fully insulated. Material is pumped to the vacuum distillation tower via centrifugal pumps (P-05A/B) (one active, one standby) at 22.5 kW / 3000 RPM. 7. Raw Naphtha Storage Unit Collects and condenses naphtha extracted during cooking. • 7-1-1: Raw Naphtha Tanks (V-07A/B/C): Three vertical Stainless Steel 304 tanks (1.5m dia, 5m H) connected to three heat exchangers and two pump pairs. Equipped internally with water spray nozzles on a ring pipe to wash non-condensable gases. • 7-1-2: Heat Exchangers (HE-01A/B/C): Condense naphtha vapors from 140°C down to 40°C using water from the cooling tower. Connected in series. Shell & Tube type, carbon steel (510 mm dia, 6m L) with 70 tubes (0.75-inch dia) in two rows of 35. Includes internal baffles for efficiency. • 7-1-3: Supporting Pumps: Vacuum pumps (VP-01A/B) at 22.5 kW / 1500 RPM draw naphtha vapors from reactors to the heat exchangers, pushing non-condensable gases to the scrubber (V-14). Centrifugal pumps (P-02A/B) at 11.5 kW / 1500 RPM transport liquid raw naphtha to the Bleaching Unit. 8. Vacuum Distillation Unit The core of the plant, separating remaining light compounds and producing hard asphalt. • 8-1-1: Vacuum Distillation Tower: A vertical tower (~16m total height, 14mm carbon steel). Bottom section (Reboiler) is 3.5m dia x 1.2m H; top section is 1.5m dia x 12m H. Fully insulated. Fed with cooked material at 190-200°C via pumps (P-05A/B). To start extraction (remaining naphtha, Gas Oil, diesel), temperature is raised to 240-250°C using Heating Coil 1 via pumps (P-08A/B) at 55 kW / 3000 RPM, with continuous circulation via pumps (P-07A/B). Vacuum pumps (VP-03A/B) maintain 0.3-0.5 mbar pressure. Light compounds are extracted, condensed (HE-02A/B/C), and stored (V-08/09/10 A/B) over 2.5-3 hours. Afterward, material is heated via Heating Coil 2 to 320-340°C to finalize extraction and produce hard bitumen. Product is extracted via pumps (P-07A/B) at ~320°C, cooled via cooling tower coils, and sent to final tanks (V-18A/B/C). Batch processing takes 6-7 hours daily; continuous operation is possible. • 8-1-2: Supporting Pumps: Vacuum pumps (VP-03A/B) at 5.5 kW / 3000 RPM draw light vapors for condensation. Circulation centrifugal pumps (P-08A/B) at 55 kW move hot material to heating coils; (P-07A/B) circulate material and pump final bitumen product. • 8-1-3: Heating Coils 1 & 2: Carbon steel 4-inch diameter coils heated externally by a Gas Oil burner. Connected in series to heat liquid bitumen in two stages to prevent degradation. • 8-2: Heat Exchangers (HE-02A/B/C): Condense light compound vapors from 240°C to 40°C. Shell & Tube type, carbon steel (600 mm dia, 6m L) with 80 tubes (1-inch dia) in two rows of 40, equipped with baffles. • 8-3: Light Compound Tanks (V-08A/B, V-09A/B, V-10A/B): Six horizontal carbon steel tanks (1.5m dia, 4.5m L, 14mm thick). Receive condensates, linked to heat exchangers and vacuum pumps. Liquids are pumped to the Bleaching Unit via centrifugal pumps (P-06A/B) at 7.5 kW / 1500 RPM. 9. Bleaching Unit Improves the specifications of raw light compounds for local use and marketing. • 9-1: Collection Tank (V-11): Horizontal carbon steel tank (1m dia, 2.5m L, 14mm thick) placed above the system to store and distribute light compounds to the bleaching columns. • 9-2: Bleaching Columns (V-12A/B/C): Three vertical carbon steel vessels (1m dia, 4.5m H, 14mm thick). Contain a 15 cm catalyst layer on trays to bleach raw liquids into high-quality compounds, collected in a bottom horizontal tank. The catalyst is a calcined mixture of Bentonite and Zinc Oxide granules (2-3 mm) homogenized in water, which can be reactivated with steam and 5% HCl. • 9-3: Supporting Pumps: Vacuum pumps (VP-04A/B) at 5.5 kW extract vapors to the scrubber. Centrifugal pumps (P-09A/B) at 7.5 kW push bleached liquids to final tanks. 10. Production Tanks (V-13 A-F & V-18 A-C) • Light Products: Six horizontal carbon steel tanks (2.8m dia, 9m L, 55-ton capacity). V-13A/B for light naphtha, V-13C/D for Gas Oil, V-13E/F for diesel. • Asphalt: Three vertical carbon steel tanks (V-18A/B/C) (5m dia, 9m H). Equipped with thermal oil heating coils to keep asphalt liquid. Fully insulated (90 kg/m³ glass wool, 1.8mm aluminum cover). 11. Supporting Systems • 11-1: Gas Washing (Scrubber) System: Treats non-condensable gases before atmospheric release. Contains V-14 washing tank (1m dia, 2.8m L), a 500mm Flare stack with 3 ignitors, and a 1m x 1m LPG tank (V-15) for ignition. • 11-2: Cooling Tower: Provides cooling water for heat exchangers. Galvanized pressed steel basin (16m L x 2.4m W x 2.8m H), FRP casing, top fans, water distributors, and fill media. Includes Accumulator tank V-20 (1.5m dia, 2m L) and 11 kW pushing pumps (P-14A/B). • 11-3: Thermal Oil Boilers: Includes oil tank, heating boiler, oil pumps, and heating accelerators. • 11-4: Distillation Tower Raw Boilers • 11-5: Power Generation System • 11-6: Production Laboratory • 11-7: Control and Operation Room • 11-8: Catalyst System: Contains a vertical diesel tank (1m dia, 1.5m H) with a 1 kW centrifugal pump (P-11). Two vertical carbon steel tanks (V-17A/B, 1.5m dia, 4.5m H) with an MX-03 hydromotor mixer (7.5 kW, 30 RPM). V-17A is for preparation, V-17B pumps catalyst to the reactor. ________________________________________ Catalyst Chemical Components & Formulations 1. Alumina (Al2O3): Enhances the cracking of chemical bonds in heavy bitumen chains and increases Gas Oil extraction yield. 2. Manganese Dioxide (MnO2): Accelerates the reaction, reduces reaction time, and acts as a gasoline improver. 3. Silicon Dioxide (SiO2): Increases acceleration and reduces reaction time. 4. Iron Oxides (Fe2O): Accelerates the reaction, prevents pipe corrosion, and stops sulfur and wax from sticking to pipes and pumps. Weight Ratios (WT/WT) to Produce One Barrel (200 Liters) of Catalyst: 1. Alumina: Varies by feed: 2-2.5% for Bitumen / 4-5% for Vacuum Residue (VR) / 2-2.5% for Heavy Fuel Oil (HFO). To increase Gas Oil/Diesel (Light fuel) yield, Alumina can be added up to a maximum of 10%. 2. Manganese Dioxide: 2-2.5% for HFO / 4-5% for VR and Bitumen. 3. Iron Oxides: 2-2.5% across all feeds. 4. Silicon Dioxide: 2-2.5% for HFO / 4-5% for Bitumen and VR. 5. Remaining Volume: Filled with C-oil. Note: One barrel (200 Liters) of this mixture is added for every 5 tons of HFO, VR, or Bitumen. Manufacturing Mechanism: All components are placed in a tank, initially mixed with water, and heated to 80-120°C with continuous mixing (20-30 RPM). Once foam is generated, the product is allowed to cool to 80°C. The heating process up to 120°C is repeated 3 or 4 times until foaming ceases. Finally, the temperature is raised to 150°C, and the mixture is topped off to 200 liters using C-oil. To further improve light compound specifications, Zinc Oxide (300 grams) is mixed with 20 kg of Bentonite in C-oil. This is added alongside the catalyst at a ratio of 1/5 barrel of catalyst added to the reactor.